Reciprocating Compressors for
Petroleum, Chemical, and Gas
Industry Services
API STANDARD 618
FIFTH EDITION, DECEMBER 2007
ERRATA 1: NOVEMBER 2009
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Reciprocating Compressors for
Petroleum, Chemical, and Gas
Industry Services
Downstream Segment
API STANDARD 618
FIFTH EDITION, DECEMBER 2007
ERRATA 1: NOVEMBER 2009
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Special Notes
API publications necessarily address problems of a general nature. With respect to particular circumstances, local,
state, and federal laws and regulations should be reviewed.
Neither API nor any of API's employees, subcontractors, consultants, committees, or other assignees make any
warranty or representation, either express or implied, with respect to the accuracy, completeness, or usefulness of the
information contained herein, or assume any liability or responsibility for any use, or the results of such use, of any
information or process disclosed in this publication. Neither API nor any of API's employees, subcontractors,
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accuracy and reliability of the data contained in them; however, the Institute makes no representation, warranty, or
guarantee in connection with this publication and hereby expressly disclaims any liability or responsibility for loss or
damage resulting from its use or for the violation of any authorities having jurisdiction with which this publication may
conflict.
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These publications are not intended to obviate the need for applying sound engineering judgment regarding when
and where these publications should be utilized. The formulation and publication of API publications is not intended in
any way to inhibit anyone from using any other practices.
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Any manufacturer marking equipment or materials in conformance with the marking requirements of an API standard
is solely responsible for complying with all the applicable requirements of that standard. API does not represent, warrant, or guarantee that such products do in fact conform to the applicable API standard.
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Copyright © 2007 American Petroleum Institute
Foreword
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manufacture, sale, or use of any method, apparatus, or product covered by letters patent. Neither should anything
contained in the publication be construed as insuring anyone against liability for infringement of letters patent.
Shall: As used in a standard, “shall” denotes a minimum requirement in order to conform to the specification.
Should: As used in a standard, “should” denotes a recommendation or that which is advised but not required in order
to conform to the specification.
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marked with a bar in the margin, as shown to the left of this paragraph. The bar notations in the margins are provided
as an aid to users, but API makes no warranty as to the accuracy of such bar notations.
This document was produced under API standardization procedures that ensure appropriate notification and
participation in the developmental process and is designated as an API standard. Questions concerning the
interpretation of the content of this publication or comments and questions concerning the procedures under which
this publication was developed should be directed in writing to the Director of Standards, American Petroleum
Institute, 1220 L Street, N.W., Washington, D.C. 20005. Requests for permission to reproduce or translate all or any
part of the material published herein should also be addressed to the director.
Generally, API standards are reviewed and revised, reaffirmed, or withdrawn at least every five years. A one-time
extension of up to two years may be added to this review cycle. Status of the publication can be ascertained from the
API Standards Department, telephone (202) 682-8000. A catalog of API publications and materials is published
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Suggested revisions are invited and should be submitted to the Standards Department, API, 1220 L Street, NW,
Washington, D.C. 20005, standards@api.org.
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iii
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Contents
1
Scope. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1
2
Normative References . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1
3
Definitions of Terms . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4
4
4.1
4.2
4.3
General . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
Unit Responsibility. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
Unit Conversion . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
Nomenclature . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
5
5.1
5.2
5.3
Requirements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
Dimensions. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
Statutory Requirements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
Conflicting Requirements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
6
6.1
6.2
6.3
6.4
6.5
6.6
6.7
6.8
6.9
6.10
6.11
6.12
6.13
6.14
6.15
6.16
Basic Design. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
General . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8
Bolting . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11
Calculating Cold Runout . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11
Allowable Speeds. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12
Allowable Discharge Temperature . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12
Rod and Gas Loads . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12
Critical Speeds . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 13
Compressor Cylinders . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 13
Valves and Unloaders . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 18
Pistons, Piston Rods, and Piston Rings . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 20
Crankcases, Crankshafts, Connecting Rods, Bearings and Crossheads . . . . . . . . . . . . . . . . . . . . . . . . . 22
Distance Pieces . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 23
Packing Cases and Pressure Packing. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 24
Lubrication . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 25
Materials . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 29
Nameplates and Rotation Arrows . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 36
7
7.1
7.2
7.3
7.4
7.5
7.6
7.7
7.8
7.9
7.10
7.11
Accessories . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 36
Drivers . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 36
Couplings and Guards . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 39
Reduction Gears . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 40
Belt Drives. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 41
Mounting Plates . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 41
Controls and Instrumentation. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 44
Piping and Appurtenances . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 48
Intercoolers, Aftercoolers, and Separators. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 50
Pulsation and Vibration Control. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 52
Air Intake Filters . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 65
Special Tools. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 65
8
8.1
8.2
8.3
8.4
Inspection and Testing . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 65
General . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 65
Inspection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 66
Testing . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 68
Preparation for Shipment . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 70
v
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Page
Page
9
9.1
9.2
9.3
Vendor’s Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 71
General . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .71
Proposals . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .72
Contract Data . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .73
Annex A (informative) Data Sheets. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .77
Annex B (informative) Capacity Rating and Tolerance . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .113
Annex C (informative) Piston Rod Runout. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .115
Annex D (informative) Repairs to Gray or Nodular Iron Castings. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .133
Annex E (informative) Purchaser’s Checklist . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .135
09
Annex F (normative) Vendor Drawing and Data Requirements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 139
Annex G (normative) Figures and Schematics . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .147
Annex H (informative) Materials for Major Component Parts . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .157
Annex I (informative) Distance Piece Vent, Drain and Buffer Systems to Minimize Process Gas Leakage . .159
Annex J (informative) Reciprocating Compressor Nomenclature . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .165
Annex K (informative) Inspector’s Checklist . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .169
Annex L (informative) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .171
Annex M (informative) Design Approach Work Process Flowcharts . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .173
Annex N (informative) Guideline for Compressor Gas Piping Design and Preparation for an Acoustic
Simulation Analysis . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .177
Annex O (informative) Guidelines for Sizing Low Pass Acoustic Filters . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .181
Annex P (informative) Piping and Pulsation Suppression Device Shaking Force Guidelines . . . . . . . . . . . . .183
Annex Q (informative) Compressor Components—Compliance with NACE MR0175 . . . . . . . . . . . . . . . . . . . .189
Figures
1
Plate Loaded in Tension in the Through-thickness Direction and its Area Requiring
Ultrasonic Inspection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 32
2
Plate Loaded in Bending and its Area Requiring Ultrasonic Inspection . . . . . . . . . . . . . . . . . . . . . . . . . 33
3
Axially Loaded Plate . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 33
4
Piping Design Vibration at Discrete Frequencies . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 61
A-1 Reciprocating Compressor Data Sheet (U.S. Customary Units) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .79
A-2 Reciprocating Compressor Data Sheet (SI Units) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .96
C-1 Basic Geometry with Cold Vertical Runout . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 116
C-2 Vertical Runout Geometric Relationships Based on No Rod Sag . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 116
C-3 Rod Runout Table . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 117
C-4 Rod Runout Attributable to Piston Rod Sag with Δ DROP = 0. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 119
C-5 Rod Runout Attributable to Piston Rod Sag with Δ DROP > 0. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .120
C-6A Data for Rod Runout Calculation. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 121
C-6B Rod Runout Calculation Example . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 122
C-6C Sample Printout for Rod Runout . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 125
C-7 Graphical Illustration of Rod Runout at 0.080 in. Cylinder Running Clearance . . . . . . . . . . . . . . . . . . 126
C-8 Graphical Illustration of Rod Runout at 0.060 in. Cylinder Running Clearance . . . . . . . . . . . . . . . . . . 127
C-9 Graphical Illustration of Rod Runout at 0.040 in. Cylinder Running Clearance . . . . . . . . . . . . . . . . . . 128
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Page
C-10
C-11
G-1
G-2
G-3
G-4
G-5
G-6
G-7
G-8
G-9
I-1
I-2
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I-3
J-1
L-1
M-1
M-2
M-3
O-1
P-1
P-2
P-3
P-4
P-5
Q-1
Graphical Illustration of Rod Runout at 0.020 in. Cylinder Running Clearance . . . . . . . . . . . . . . . . . .
Graphical Illustration of Rod Runout at 0.010 in. Cylinder Running Clearance . . . . . . . . . . . . . . . . . .
Cylinder Cooling System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Typical Cylinder Indicator Tap Connection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Distance Piece and Packing Arrangements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Typical Self-Contained Cooling System for Piston Rod Pressure Packing . . . . . . . . . . . . . . . . . . . . . .
Typical Pressurized Frame Lube Oil System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Conceptual Direct Rod Connection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Conceptual Indirect Rod Connection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Conceptual Indirect Clamped Rod Connection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Tightening Diagram (Bolt–Bracing–Diagram) . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Typical Buffered Single Compartment Distance Piece Vent, Drain, and Buffer Arrangement
to Minimize Process Gas Leakage . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Typical Buffered Two Compartment Distance Piece Vent, Drain, and Buffer Arrangement
to Minimize Process Gas Leakage . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Typical Purged Packing Arrangements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Reciprocating Compressor Nomenclature. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Typical Mounting Plate Arrangement . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Design Approach 1 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Design Approach 2 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Design Approach 3 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Nonsymmetrical Filter. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Non-dimensional Piping Shaking Force Guidelines . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Non-dimensional Pulsation Suppression Device Shaking Force Guidelines . . . . . . . . . . . . . . . . . . . .
Shaking Forces along the Piping Axis . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Shaking Forces along the Pulsation Suppression Device Axis . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Examples of Shaking Force Restraints . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
Material Guidelines for Compressor Components—Compliance
with NACE MR0175 . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .
129
130
149
150
151
152
153
154
154
154
155
161
162
163
167
171
173
174
175
181
183
184
184
185
187
190
Tables
1
Cooling System Conditions . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 9
2
Driver Trip Speed. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 10
3
Maximum Gauge Pressures for Cylinder Materials. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 31
4
Relief Valve Settings . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 46
5
Minimum Alarm and Shutdown Requirements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 47
6
Design Approach Selection . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 54
7
Maximum Severity of Defects in Castings . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 67
E-1 Purchaser’s Checklist. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 135
H-1 Material Specifications for Reciprocating Compressor Parts . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 157
K-1 Inspector’s Checklist . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 169
N-1 Compressor Data Required for Acoustic Simulation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 179
P-1 Cylinder Assembly Weights Possibly Requiring Strengthening . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 187
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Reciprocating Compressors for Petroleum, Chemical, and Gas Industry Services
Introduction
This standard is based on the accumulated knowledge and experience of manufacturers and users of reciprocating compressors.
The objective of this publication is to provide a purchase specification to facilitate the procurement and manufacture of
reciprocating compressors for use in petroleum, chemical, and gas industry services.
The primary purpose of this standard is to establish minimum requirements.
Energy conservation is of concern and has become increasingly important in all aspects of equipment design, application, and
operation. Thus, innovative energy-conserving approaches should be aggressively pursued by the manufacturer and the user
during these steps. Alternative approaches that may result in improved energy utilization should be thoroughly investigated and
brought forth. This is especially true of new equipment proposals since the evaluation of purchase options will be based
increasingly on total life costs as opposed to acquisition cost alone.
Equipment manufacturers, in particular, are encouraged to suggest alternatives to those specified when such approaches achieve
improved energy effectiveness and reduced total life costs without the sacrifice of safety or reliability.
This standard requires the purchaser to specify certain details and features. Although it is recognized that the purchaser may desire
to modify, delete, or amplify sections of this standard, it is strongly recommended that such modifications, deletions, and
amplifications be made by supplementing this standard, rather than by rewriting or incorporating sections thereof into another
standard.
For effective use of this standard and ease of reference to the text, the use of the data sheets in Annex A is recommended.
Users of this standard should be aware that further or differing requirements may be needed for individual applications. This
standard is not intended to inhibit a vendor from offering, or the purchaser from accepting, alternative equipment or engineering
solutions for the individual application. This may be particularly applicable where there is innovative or developing technology.
Where an alternative is offered, the vendor should identify any variations from this standard and provide details.
1 Scope
This standard covers the minimum requirements for reciprocating compressors and their drivers for use in petroleum, chemical,
and gas industry services for handling process air or gas with either lubricated or non-lubricated cylinders.
Compressors covered by this standard are low to moderate speed machines. Also included are related lubrication systems,
controls, instrumentation, intercoolers, aftercoolers, pulsation suppression devices, and other auxiliary equipment. Compressors
not covered by this standard are (a) integral gas-engine-driven compressors, (b) compressors with single-acting trunk-type
(automotive-type) pistons that also serve as crossheads, and (c) either plant or instrument-air compressors that discharge at a
gauge pressure of 9 bar (125 psig) or below.
Note 1: Requirements for packaged high-speed reciprocating compressors for oil and gas production services are covered in ISO 13631.
Note 2: A bullet (•) at the beginning of a clause indicates that either a decision is required or further information is to be provided by the
purchaser. This information should be indicated on the data sheets (see Annex A); otherwise it should be stated in the quotation request (inquiry)
or in the order.
2 Normative References
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2.1 The following referenced documents are indispensable for the application of this document. For dated references, only the
edition cited applies. For undated references, the latest edition of the referenced document (including any amendments) applies.
API
RP 500
Std 541
Std 546
Std 611
Std 612
Classification of Locations for Electrical Installation at Petroleum Facilities Classified as Class I,
Division 1 and Division 2
Form-wound Squirrel-cage Induction Motors—500 Horsepower and Larger
Brushless Synchronous Machines—500 kVA and Larger
General Purpose Steam Turbines for Petroleum, Chemical and Gas Industry Services
Petroleum, Petrochemical and Natural Gas Industries—Steam Turbines—Special-purpose Applications
1
2
API STANDARD 618
Std 613
Std 614
Std 616
Std 670
Std 671
Std 677
RP 686
Special Purpose Gear Units for Petroleum, Chemical and Gas Industry Services
Lubrication, Shaft-sealing, and Control-oil Systems and Auxiliaries for Petroleum, Chemical and Gas Industry
Services
Gas Turbines for the Petroleum, Chemical and Gas Industry Services
Machinery Protection Systems
Special-Purpose Couplings for Petroleum, Chemical and Gas Industry Services
General-Purpose Gear Units for Petroleum, Chemical and Gas Industry Services
Recommended Practices for Machinery Installation and Installation Design
Measurement of Petroleum Measurement Standards (MPMS)
Ch. 15
Guidelines for Use of the International System of Units (SI) in the Petroleum and Allied Industries
AGMA1
9002
ANSI2
S2.19
ASME3
B1.1
B16.1
B16.5
B16.11
B16.42
B16.47
B31.3
Bores and Keyways for Flexible Couplings (Inch Series)
Mechanical Vibration-Balance Quality Requirements of Rigid Motors—Part 1: Determination of
Possible Unbalance, Including Marine Applications
Unified Inch Screw Threads (UN & UNR Thread Form)
Gray Iron Pipe Flanges and Flanged Fittings: Classes 25, 125, and 250
Pipe Flanges and Flanged Fittings NPS 1/2 through NPS 24 Metric/Inch Standard
Forged Fittings, Socket-Welding and Threaded
Ductile Iron Pipe Flanges & Flanged Fittings: Classes 150 and 300
Large Diameter Steel Flanges
Process Piping
Boiler and Pressure Vessel Code
Section V, “Nondestructive Examination”
Section VIII, Division 1, “Rules for Construction of Pressure Vessels”
Section IX, “Welding and Brazing Qualifications”
ASTM4
A 193
A 194
A 216
A 247
A 278
A 307
A 320
A 388
A 395
A 503
A 515
A 668
Standard Specification for Alloy-Steel and Stainless Steel Bolting Materials for High Temperature or High
Pressure Service and other Special Purpose Applications
Standard Specification for Carbon and Alloy Steel Nuts for Bolts for High Pressure or High Temperature
Service, or Both
Standard Specification for Steel Castings, Carbon, Suitable for Fusion Welding, for High Temperature
Service
Standard Test Method for Evaluating the Microstructure of Graphite in Iron Castings
Standard Specification for Gray Iron Castings for Pressure-Containing Parts for Temperatures up to 650°F
(350°C)
Standard Specification for Carbon Steel Bolts and Studs, 60 000 PSI Tensile Strength
Standard Specification for Alloy-Steel And Stainless Steel Bolting Materials for Low-Temperature Service
Standard Practice for Ultrasonic Examination of Heavy Steel Forgings
Standard Specification for Ferritic Ductile Iron Pressure-Retaining Castings for Use at Elevated
Temperatures
Standard Specification for Ultrasonic Examination of Forged Crankshafts
Standard Specification for Pressure Vessel Plates, Carbon Steel, for Intermediate
and Higher-Temperature Service
Standard Specification for Steel Forgings, Carbon and Alloy, for General Industrial Use
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1American Gear Manufacturers Association, 500 Montgomery Street, Suite 350, Alexandria, Virginia 22314-1581, www.agma.org.
2American National Standards Institute, 25 West 43rd Street, 4th floor, New York, New York 10036, www.ansi.org.
3ASME International, Three Park Avenue, New York, New York 10016-5990, www.asme.org.
4ASTM International, 100 Barr Harbor Drive, West Conshohocken, Pennsylvania 19428-2959, www.astm.org.
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
E 94
E 125
E 165
E 709
AWS5
D 1.1
3
Standard Guide for Radiographic Examination
Standard Reference Photographs for Magnetic Particle Indications on Ferrous Castings
Standard Test Method for Liquid Penetrant Examination
Standard Guide for Magnetic Particle Examination
Structural Welding Code—Steel
IEC6
60034 (all parts) Rotating Electrical Machines
60079 (all parts) Electrical Apparatus for Explosive Gas Atmospheres
60529
Degrees of Protection Provided by Enclosures (IP Code)
60848
GRAFCET Specification Language for Sequential Function Charts
Pipe threads where pressure-tight joints are made on the threads—Part 1: Dimensions, tolerances and
designation
7-2
Pipe threads where pressure-tight joints are made on the threads—Part 2: Verification by means of limit
gauges
261
ISO General-purpose metric screw threads—General plan
262
ISO General-purpose metric screw threads—Selected sizes for screws, bolts and nuts
281
Rolling bearings—Dynamic load ratings and rating life
286-2
ISO system of limits and fits—Part 2: Tables of standard tolerance grades and limit deviations for
holes and shafts
724
ISO General purpose metric screw threads—Basic dimensions
965 (all parts) ISO General purpose metric screw threads—Tolerances
1217
Displacement compressors—Acceptance tests
1940-1
Mechanical vibration—Balance quality requirements for rotors in a constant (rigid) state—Part 1:
Specification and verification of balance tolerances
6708
Pipework components—Definition and selection of DN (Nominal Size)
7005-1
Metallic flanges—Part 1: Steel flanges
7005-2
Metallic flanges—Part 2: Cast iron flanges
7005-3
Metallic flanges—Part 3: Copper alloy and composite flanges
8501 (all parts) Preparation of steel substrates before application of paints and related products—Visual assessment of
surface cleanliness
10441
Petroleum and natural gas industries—Flexible couplings for mechanical power transmission—Special
purpose applications
10437
Petroleum, petrochemical and natural gas industries—Steam turbines—Special-purpose applications
10438 (all parts) Petroleum, petrochemical and natural gas industries—Lubrication, shaft-sealing and control-oil systems
and auxiliaries
10816-6
Mechanical vibration—Evaluation of machine vibration by measurements on non-rotating parts—Part 6:
reciprocating machines with power ratings above 100 kW
13631
Petroleum and natural gas industries—Packaged reciprocating gas compressors
13691
Petroleum and natural gas industries—High-speed special-purpose gear units
14691
Petroleum and natural gas industries—Flexible couplings for mechanical power transmission—General
purpose applications
16889
Hydraulic fluid power filters—Multi-pass method for evaluating filtration performance of a filter element
NACE8
Corrosion Engineer’s Reference Book
5American Welding Society, 550 N.W. LeJeune Road, Miami, Florida 33126, www.aws.org.
6International Electrotechnical Commission, 3, rue de Varembe, P.O. Box 131, CH-1211 Geneva 20, Switzerland, www.iec.ch.
7International Organization for Standardization, 1, ch. de la Voie-Creuse, Case postale 56, CH-1211 Geneva 20, Switzerland, www.iso.ch.
8NACE International, 1440 South Creek Drive, Houston, Texas 77084-4906, www.nace.org.
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ISO7
7-1
4
API STANDARD 618
MR0175
Petroleum and Natural Gas Industries—Materials for use in H2S-Containing Environments in Oil and Gas
Production
NEMA9
MG 1
Motors and Generators
NFPA10
70
National Electrical Code
SSPC11
SP 6/NACE No. 3
Commercial Blast Cleaning
2.2 “Notes” following a clause are informative.
The equipment supplied to this standard shall comply with either the applicable ISO standards or the applicable U.S.
• 2.3
standards, as specified.
3 Definitions of Terms
For the purposes of this document, the following terms and definitions apply:
3.1 acoustic simulation: The process whereby the one-dimensional acoustic characteristics of fluids and the influence of the
reciprocating compressor dynamic flow on these characteristics are modeled, taking into account the fluid properties and the
geometry of the compressor and the connected vessels and piping.
Note: The model is mathematically based upon the governing differential equations (motion, continuity, etc.). The simulation should allow for
determination of pressure/flow modulations at any point in the piping model resulting from any generalized compressor excitation (see 3.1, 3.4,
3.9, 3.28, 3.39, and 3.57).
3.2 active analysis: A portion of the acoustic simulation in which the pressure pulsation amplitudes, due to imposed
compressor operation for the anticipated loading, speed range, and state conditions, are simulated (see 3.1).
3.3 alarm point: A preset value of a measured parameter at which an alarm is actuated to warn of a condition that requires
corrective action.
3.4 analog simulation: A method using electrical components (inductances, capacitances, resistances and current supply
devices) to achieve the acoustic simulation (see 3.1).
3.5 anchor bolts: Bolts used to attach the mounting plate or machine to the support structure (concrete foundation or steel
structure).
Note: See 3.13 for definition of hold down bolts. Also see Figure L-1.
3.6 baseplate: A fabricated steel structure designed to provide support to the complete compressor and/or the drive
equipment and other ancillaries which may be mounted upon it.
3.7 combined rod load: The algebraic sum of gas load and inertia force on the crosshead pin.
Note: Gas load is the force resulting from differential gas pressure acting on the piston differential area. Inertia force is the force resulting from
the acceleration of reciprocating mass. The inertia force with respect to the crosshead pin is the summation of the products of all reciprocating
masses (piston and rod assembly, and crosshead assembly including pin) and their respective acceleration.
3.8 design: A term that may be used by the equipment manufacturer to describe various parameters such as design power,
design pressure, design temperature, or design speed.
Note: This terminology should be used only by the equipment manufacturer and not in the purchaser’s specifications.
3.9 digital simulation: A method using various mathematical techniques on digital computers to achieve the acoustic
simulation (see 3.1).
9National Electrical Manufacturers Association, 1300 North 17th Street, Suite 1752, Rosslyn, Virginia 22209, www.nema.org.
10National Fire Protection Association, 1 Batterymarch Park, Quincy, Massachusetts 02169-7471, www.nfpa.org.
11The Society for Protective Coatings, 40 24th Street, 6th Floor, Pittsburgh, Pennsylvania 1522-4656, www.sspc.org.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
5
3.10 drive train: Includes all drive equipment up to the compressor shaft free-end and all components coupled to the free-end
of the crankshaft.
3.11 fail safe: A system which causes the equipment to revert to a permanently safe condition (shutdown and/or
depressurized) in the event of a component failure or failure of the energy supply to the system.
3.12 gauge board: A bracket or plate used to support and display gauges, switches, transmitters, and other instruments. A
gauge board is open and not enclosed.
Note: A gauge board is not a panel. A panel is an enclosure. See 3.35 for the definition of a panel.
3.13 hold down bolts (mounting bolts): Bolts holding the equipment to the mounting plate.
3.14 informative: Describes part of the standard that is provided for information and is intended to assist in the understanding
of use of the standard.
Note 1: Compliance with an informative part of the standard is not mandatory.
Note 2: An annex may be informative or normative as indicated. See 3.32 for definition of normative.
3.15 inlet volume flow: The flow rate expressed in volume flow units at the conditions of pressure, temperature,
compressibility and gas composition, including moisture content, at the compressor inlet flange. To determine inlet volume flow,
allowance must be made for pressure drop across pulsation suppression devices and for interstage liquid knockout.
Note: Inlet volume flow is a specific example of actual volume flow. Actual volume flow is the volume flow at any particular location such as
interstage, compressor inlet flange or compressor discharge. Therefore, actual volume flow should not be used interchangeably with inlet
volume flow.
3.16 local: The location of a device when mounted on or near the equipment or console.
3.17 manufacturer: The organization responsible for the design and manufacture of the equipment.
Note: The manufacturer is often a different entity from the vendor.
3.18 manufacturer’s rated capacity: The capacity used to size the compressor, which is the quantity of gas, taken into the
compressor cylinder at the specified inlet conditions, while the compressor is operating at the specified discharge pressure.
Note: See 3.43, 3.48, and 6.1.3.
3.19 maximum allowable continuous combined rod load: The highest combined rod load at which none of the forces
in the running gear (piston, piston rod, crosshead assembly, connecting rod, crankshaft, bearings etc.) and the compressor frame
exceed the values in any component for which the manufacturer’s design permits continuous operation.
3.20 maximum allowable continuous gas load: The highest force that a manufacturer permits for continuous operation
on the static components (e.g., frame, distance piece, cylinder and bolting) of the compressor.
3.21 maximum allowable speed: The highest rotational speed at which the manufacturer’s design permits continuous
operation.
3.23 maximum allowable working pressure (MAWP): The maximum continuous gauge pressure for which the
manufacturer has designed the equipment (or any part to which the term is referred) when handling the specified fluid at the
specified maximum operating temperature.
3.24 maximum continuous speed: The highest rotational speed at which the machine, as built, is capable of continuous
operation with the specified fluid at any of the specified operating conditions.
3.25 minimum allowable speed: The lowest rotational speed at which the manufacturer’s design permits continuous
operation.
3.26 minimum allowable suction pressure (for each stage): The lowest pressure (measured at the inlet flange of the
cylinder) below which the combined rod load, gas load, discharge temperature, or crankshaft torque load (whichever is
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3.22 maximum allowable temperature: The maximum continuous temperature for which the manufacturer has designed
the equipment (or any part to which the term is referred) when handling the specified fluid at the specified maximum operating
pressure.
6
API STANDARD 618
governing) exceeds the maximum allowable value during operation at the set pressure of the discharge relief valve and other
specified inlet gas conditions for the stage.
3.27 minimum allowable temperature: The lowest temperature for which the manufacturer has designed the equipment
(or any part to which the term is referred).
3.28 mode shape (of an acoustic pulsation resonance): The description of the pulsation amplitudes and phase angle
relationship at various points in the piping system. Knowledge of the mode shape allows the analyst to understand the pulsation
patterns in the piping system (see 3.1).
3.29 mounting plate: Baseplates, skids, soleplates, and rails.
3.30 normal operating point: The point at which usual operation is expected and optimum efficiency is desired. This point
is usually the point at which the manufacturer certifies that performance is within the tolerances stated in this standard.
3.31 normally open and normally closed: Refers both to the on-the-shelf state and to the installed, de-energized state of
devices such as automatically controlled electrical switches and valves.
Note: The normal operating state of such devices is not necessarily the same as the on-the-shelf state.
3.32 normative: A requirement to be met in order to comply with the standard.
3.33 observed: An inspection or test where the purchaser is notified of the timing of the inspection or test and the inspection
or test is performed, as scheduled, even if the purchaser or the purchaser’s representative is not present.
3.34 owner: The final recipient of the equipment.
Note: In many instances the owner delegates another agent to be the purchaser of the equipment.
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3.35 panel: An enclosure used to mount, display, and protect gauges, switches and other instruments.
3.36 passive analysis: A portion of the acoustic simulation in which a constant flow amplitude modulation over an arbitrary
frequency range is imposed on the system, normally at the cylinder valve locations. The resulting transfer function defines the
acoustic natural frequencies and the mode shapes over the frequency range of interest (see 3.1).
3.37 piston rod drop: A measurement of the position of the piston rod relative to the measurement probe mounting
location(s) (typically oriented vertically at the pressure packing on horizontal cylinders).
3.38 piston rod runout: The change in position of the piston rod in either the vertical or horizontal direction as measured at
a single point (typically at or near the pressure packing case) while the piston rod is moved through the outbound portion of its
stroke.
Note 1: In horizontal compressors, the piston rod runout is measured in both the vertical and horizontal directions. Horizontal runout is taken on
the side of the rod to determine horizontal variations, while vertical runout is taken on the top of the rod to determine vertical variations.
Note 2: Practical considerations make it advisable to monitor the runout measurements while rotating the shaft through one complete revolution.
Note 3: See Annex C for a detailed discussion of piston rod runout.
3.39 pressure casing: The composite of all stationary pressure containing parts of the unit, including all nozzles and other
attached parts.
3.40 pressure design code: The recognized pressure vessel standard specified or agreed upon by the purchaser. Example:
A recognized standard for pressure vessels is ASME Section VIII.
3.41 purchaser: The agency that issues the order and specification to the vendor.
Note: The purchaser may be the owner of the plant in which the equipment is to be installed or the owner’s appointed agent.
3.42 rails: Soleplates extending the full length of each side of the equipment.
3.43 rated discharge pressure: The highest pressure required to meet the conditions specified by the purchaser for the
intended service.
3.44 rated discharge temperature: The highest predicted operating temperature resulting from any specified operating
condition.
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
7
3.45 rated speed: The highest rotational speed required to meet any of the specified operating conditions.
3.46 relief valve set pressure: The pressure at which a relief valve starts to lift.
3.47 remote: The location of a device when located away from the equipment or console, typically in a control room.
3.48 required capacity: The process capacity specified by the purchaser to meet process conditions, with no-negativetolerance (NNT) permitted.
Note 1: The required capacity is the quantity of gas taken into the compressor cylinder at the specified inlet conditions while the compressor is
operating at the specified discharge pressure and speed.
Note 2: See Annex B for an explanation of the term no-negative tolerance.
3.49 rod reversal: A change in direction of force in the piston rod loading (tension to compression or vice-versa), which
results in a load reversal at the crosshead pin during each revolution.
3.50 settling-out pressure: The pressure within the compressor system when the compressor is shut down without
depressuring of the system.
3.51 shall: Is used to state a mandatory requirement.
3.52 shutdown set point: A preset value of a measured parameter at which automatic or manual shutdown of the system or
equipment is required.
3.53 skid: A baseplate that has sled-type runners for ease of relocation.
3.54 soleplates: Grouted plates installed under motors, bearing pedestals, gearboxes, turbine feet, cylinder supports,
crosshead pedestals and compressor frames (see Annex L).
3.55 special tool: A tool that is not a commercially available catalog item.
3.56 standard volume flow: The flow rate expressed in volume flow units at either of the standard conditions outlined:
SI flow units are typically:
Normal cubic meters per hour (Nm3/h), or
Normal cubic meters per minute (Nm3/min)
At ISO standard conditions of
Absolute pressure: 1.013 bar
Temperature: 0°C
U.S. customary flow units are typically:
Standard cubic feet per minute (scfm), or
Million standard cubic feet per day (mmscfd)
At customary standard conditions of
Absolute pressure: 14.7 psia
Temperature: 60°F
3.57 spectral frequency distribution: The description of the pressure pulsation harmonic amplitudes versus frequency at a
selected test point location for an active or passive acoustic analysis (see 3.1).
3.58 total indicator reading (TIR), (also known as total indicated runout): The difference between the maximum
and minimum readings of a dial indicator or similar device, monitoring a face or cylindrical surface during one complete
revolution of the monitored surface.
Note: For a cylindrical surface, the indicator reading implies an eccentricity equal to half the reading. For a perfectly flat face, the indicator
reading gives an out-of-squareness equal to the reading. If the diameter in question is not cylindrical or flat, interpretation of the TIR is more
complex and can be affected by ovality or lobing.
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API STANDARD 618
3.59 trip speed: The speed at which the independent emergency overspeed device actuates to shutdown a variable-speed
prime mover. For the purposes of this standard, the trip speed of alternating current electric motors, except variable frequency
drives, is the speed corresponding to the synchronous speed of the motor at the maximum supply frequency (see Table 2).
3.60 unit responsibility: The responsibility for coordinating the manufacturing and technical aspects of the equipment and
all auxiliary systems included in the scope of the order.
Note: The technical aspects to be considered include, but are not limited to, the power requirements, speed, rotation, general arrangement,
couplings, dynamics, noise, lubrication, sealing system, material test reports, instrumentation, piping, conformance to specifications, and testing
of components.
3.61 vendor (also known as supplier): The agency, company, or entity that supplies the equipment.
Note 1: The vendor can be the manufacturer of the equipment or the manufacturer’s agent and normally is responsible for service support.
Note 2: The API mechanical equipment documents address the responsibilities between two parties. For the purposes of these standards, these
parties are defined as the purchaser (see 3.41) and the vendor or supplier (see 3.61). There are many parties that are involved in the purchase and
manufacture of the equipment. These parties are given different titles depending on the location in the chain of the order. They may be called
buyer, contractor, manufacturer, and sub-vendor. In all instances, however, one party is purchasing something from another party. For example,
the party supplying a lube oil console may be the console vendor to the compressor manufacturer, the sub-vendor to the purchaser, and the
purchaser of components within the console. All of these terms can be reduced to the purchaser and vendor or supplier. It is for this reason that
only these two terms are used in the body of the standard.
3.62 witnessed: An inspection or test where the purchaser is notified of the timing of the inspection or test and a hold is
placed on the inspection or test until the purchaser or the purchaser’s representative is in attendance.
4 General
4.1 UNIT RESPONSIBILITY
The vendor who has unit responsibility shall ensure that all sub-vendors comply with the requirements of this standard and all
referenced documents.
4.2 UNIT CONVERSION
The factors in API MPMS, Chapter 15, were used to convert from U.S. customary to SI units. The resulting exact SI units were
then rounded off.
4.3 NOMENCLATURE
A guide to reciprocating compressor nomenclature is presented in Annex J.
5 Requirements
• 5.1
DIMENSIONS
The data, drawings, hardware (including fasteners) and equipment supplied to this standard shall use either the SI or U.S.
customary system of measurement, as specified.
The purchaser and the vendor shall mutually determine the measures that must to be taken to comply with any governmental
codes, regulations, ordinances, or rules that are applicable to the equipment.
5.3 CONFLICTING REQUIREMENTS
In case of conflict between this standard and the inquiry, the inquiry shall govern. At the time of the order, the order shall govern.
6 Basic Design
6.1 GENERAL
6.1.1 The equipment (including auxiliaries) covered by this standard shall be designed and constructed for a minimum service
life of 20 years and at least three years of uninterrupted operation. Achieving these targets is the shared responsibility of the
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5.2 STATUTORY REQUIREMENTS
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
9
purchaser and vendor and depends on the process system design. It is understood that interruptions to the continuous operation
may occur due to exceeding the lifetime of wearing parts.
Note: It is recognized that these are design criteria.
6.1.2 The vendor shall assume unit responsibility for all equipment and all auxiliary systems included in the scope of the order.
•
6.1.3 The equipment’s normal operating point shall be as specified. Unless otherwise specified, the capacity at the normal
operating point shall have no negative tolerance (see 3.18, 3.30, and 3.48).
Note: See Annex B for a discussion of capacity and the term “no negative tolerance.”
6.1.4 Compressors driven by induction motors shall be rated at the actual motor speed for the rated load condition, not at
synchronous speed.
6.1.5 The pressure design code shall be specified or agreed upon by the purchaser.
6.1.6 Control of the sound pressure level (SPL) of all equipment furnished shall be a joint effort of the purchaser and the vendor
having unit responsibility. The equipment furnished by the vendor shall conform to the maximum allowable sound pressure level
specified.
In order to determine compliance, the vendor shall provide both maximum sound pressure and sound power level data per octave
band for the equipment.
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•
•
Note: The sound power level of a source can be treated as a property of that source under a given set of operating conditions. The sound pressure
level, however, will vary depending on the environment in which the source is located as well as the distance from the source. Vendors routinely
take exception to guaranteeing a purchaser’s maximum allowable sound pressure level requirements due to the argument that the vendor has no
control over the environment in which the equipment is to be located. The vendor has control, however, over the sound power level of the
equipment.
6.1.7 Unless otherwise specified, the cooling water system or systems shall, as a minimum, be designed for the conditions of
Table 1.
Table 1—Cooling System Conditions
Parameter
Requirement
For Heat Exchanger
SI Units
USC Units
Velocity over exchanger surfaces
1.5 m/s – 2.5 m/s
(5 ft/s – 8 ft/s)
Maximum allowable working pressure (MAWP)
>7 bar (gauge)
(100 psig)
Test pressure (>1.5 MAWP)
10.5 bar (gauge)
(150 psig)
Maximum pressure drop
1 bar
(15 psi)
Maximum inlet temperature
30°C
(90°F)
Maximum outlet temperature
50°C
(120°F)
Maximum temperature rise
20K
(30°F)
Minimum temperature rise
10K
(20°F)
Water side fouling factor
0.35 m2 K/kW
(0.002 hr-ft2 °F/Btu)
Corrosion allowance for carbon steel shells
3 mm
(0.125 in.)
For Cylinder Jackets and Packing Cases
Maximum allowable working pressure (MAWP)
>5 bar (gauge)
(75 psig)
Test pressure (>1.5 MAWP)
7.5 bar (gauge)
(112.5 psig)
To avoid condensation, the minimum inlet water temperature to water cooled bearing housings should preferably be above
the ambient air temperature.
The vendor shall notify the purchaser if the criteria for minimum temperature rise and velocity over heat exchange surfaces results
in a conflict. The criterion for velocity over heat exchange surfaces is intended to minimize water-side fouling. The criterion for
minimum temperature rise is intended to minimize the use of cooling water. The final selection shall be subject to purchaser’s
approval.
Note: The purchaser should specify the requirements for cooling systems when they are different than those listed in Table 1.
10
API STANDARD 618
Provisions shall be made for complete venting and draining of the cooling water system.
6.1.8 Equipment shall be designed to run simultaneously at the relief valve settings and trip speed without damage.
Note: There can be insufficient driver power to operate under these conditions (see 7.1.1).
6.1.9 The equipment's trip speed shall not be less than the values in Table 2.
Table 2—Driver Trip Speed
Driver Type
Steam turbine, NEMA Class Aa
Steam turbine, NEMA Classes B, C, Da
Gas turbine
Variable-speed motor
Constant-speed motor
Reciprocating engine
a Indicates governor classes as specified in NEMA SM 23.
Trip Speed
(percent of rated speed)
115
110
105
110
100
110
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6.1.10 Reciprocating compressors should normally be specified for constant-speed operation in order to avoid excitation of
torsional, acoustic, and/or mechanical resonances. When variable-speed drivers are used, all equipment shall be designed to run
safely throughout the operating speed range, up to and including the trip speed. For variable-speed drives, a list of undesirable
running speeds shall be furnished to the purchaser by the vendor. The occurrence of undesirable speeds in the operating range
shall be minimized.
Note: Valve life may be affected if a wide operating speed range is specified.
6.1.11 The arrangement of the equipment, including piping and auxiliaries, shall be developed jointly by the purchaser and the
vendor. The arrangement shall provide adequate clearance areas and safe access for operation and maintenance.
•
6.1.12 Motors, electrical components, and electrical installations shall be suitable for the area classification (class, group,
division, or zone) specified and shall meet the requirements of IEC 60079 (or NFPA 70, Articles 500, 501, 502, and 504), as well
as any local codes as specified and furnished on request by the purchaser.
6.1.13 Oil reservoirs and housings that enclose moving lubricated parts such as bearings, shaft seals, highly polished parts,
instruments, and control elements, shall be designed to minimize contamination by moisture, dust, and other foreign matter
during periods of operation and idleness.
6.1.14 All equipment shall be designed to permit rapid and economical maintenance. Major parts such as cylinders, distance
pieces, and compressor frames shall be designed and manufactured to ensure accurate alignment on re-assembly. This can be
accomplished by such methods as shouldering, using cylindrical dowels, or keys.
6.1.15 After installation, the performance of the combined units shall be the joint responsibility of the purchaser and the vendor
who has unit responsibility.
6.1.16 Many factors can adversely affect site performance. These factors include piping loads, alignment at operating
conditions, supporting structure, handling during shipment, and handling and assembly at the site. To minimize the influence of
these factors, the vendor shall review and comment on the purchaser’s piping and foundation drawings in accordance with the
agreed schedule. This review shall not imply that the vendor has design responsibility for the content of the purchaser’s drawings.
The vendor’s review of foundation drawings shall be limited to anchor bolt layout and the vendor’s input data used for foundation
design.
• 6.1.17
When specified, the purchaser and the manufacturer shall agree on the details of an initial installation check by the
vendor’s representative and an operating temperature alignment check at a later date. Such checks shall include, but not be limited
to, initial alignment check, grouting, crankshaft web deflection, piston-rod runout, driver alignment, motor air gap, outboard
bearing insulation, bearing checks, and piston end clearance.
6.1.18 The power required by the compressor at the normal operating point shall not exceed the stated power by more than 3%.
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
11
6.1.19 Compressors shall be capable of developing the maximum differential pressure specified (e.g., minimum specified
suction to maximum specified discharge pressure).
• 6.1.20
The equipment, including all auxiliaries, shall be suitable for operation under the environmental conditions specified.
These conditions shall include whether the installation is indoors (heated or unheated) or outdoors (with or without a roof),
maximum and minimum temperatures, unusual humidity, and dusty or corrosive conditions. The degree of winterization and/or
tropicalization (e.g., allowances for insulation) shall be mutually agreed upon by the purchaser and the vendor.
• 6.1.21
• 6.1.22
The equipment, including all auxiliaries, shall be suitable for operation using the utility stream conditions specified.
The purchaser shall specify flow, gas composition, and gas conditions. The purchaser can also specify molecular weight,
ratio of specific heats (Cp/Cv), and compressibility factors (Z).
At discharge conditions, mass flow shall reflect leakage, liquid condensation, and the work of compression.
6.1.23 Unless otherwise specified, the vendor shall use the specified values of flow, the specified gas composition, and the
specified gas conditions to calculate molecular weight, ratio of specific heats (Cp/Cv), and compressibility factors (Z). The
compressor vendor shall indicate his values on the data sheets with the proposal and use them to calculate performance data.
Note: The dew point of the gas is particularly important in non-lubricated applications.
6.1.24 If any of the compressor cylinders are to be operated partially or fully unloaded for extended periods of time, the
purchaser and the vendor shall jointly determine the method to be used (e.g., periodic, momentary loading to purge accumulation
of lube oil in the compressor cylinders) to prevent heat and liquid damage.
6.1.25 The compressor vendor shall confirm that the unit is capable of continuous operation at any full-load, part-load, or fully
unloaded conditions (see 6.1.24) and that the unit is capable of start-up in accordance with 7.1.1.6.
6.1.26 Spare parts and replacement parts for the machine and all furnished auxiliaries shall meet all the requirements of this
standard.
Note: See 9.3.6 for parts list requirements.
6.2 BOLTING
6.2.1 Details of threading shall conform to ISO 261, ISO 262, ISO 724, and ISO 965 or ASME B1.1. The use of fine pitch
threads shall be avoided in external fasteners subject to routine maintenance, fasteners for pressure retaining parts, and fasteners
in cast iron. Fasteners of diameters equal to or greater than 24 mm (1 in.) shall be of the constant 3 mm pitch (8 threads/in.) series.
6.2.2 Adequate clearance shall be provided at all bolting locations to permit the use of socket or box wrenches.
6.2.3 Internal socket-type, slotted-nut, or spanner-type bolting shall not be used unless specifically approved by the purchaser.
Note: For limited space locations, an integrally flanged fastener may be required.
6.2.4 Manufacturer’s marking shall be located on all fasteners 6 mm (1/4 in.) and larger (excluding washers and headless
setscrews). For studs, the marking shall be on the nut end of the exposed stud end.
Note: A setscrew is a headless screw with an internal hex opening on one end.
6.2.5 Bolting on reciprocating or rotating parts shall be positively locked mechanically (spring washers, tab washers, and
anaerobic adhesives shall not be used as positive locking methods) (see 6.10.2.1).
6.3 CALCULATING COLD RUNOUT
6.3.1 For horizontal compressors, the vendor shall calculate the vertical cold runout, including rod sag (as outlined in Annex C
or by other proprietary methods). These values and a runout table (see Annex C) shall be submitted to the purchaser before the
shop bar-over test. The manufacturer shall disclose the details of his calculations and the assumptions on which they are based.
The shop-measured horizontal and vertical cold rod runout shall equal the predicted cold rod runout within a tolerance of
±0.015% of stroke. Horizontal (side) piston rod runout, as measured by dial indicators during the shop bar-over test, shall not
exceed 0.064 mm (0.0025 in.), regardless of length of stroke (see 8.3.4.1). See 6.10.4.6 when tail rod construction is used. Piston
rod runout shall be measured adjacent to the cylinder packing case flange. See Annex C for clarification of rod runout and typical
rod runout table.
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API STANDARD 618
6.3.2 For non-horizontal cylinders, the procedures and tolerances for runout measurements shall be mutually agreed upon
between the purchaser and vendor.
6.3.3 Reciprocating compressor installations shall be designed in accordance with API 686, and compressors shall be installed
in accordance with API 686.
• 6.4
ALLOWABLE SPEEDS
Compressors shall be conservatively rated at a speed less than or equal to that known by the manufacturer to result in low
maintenance and trouble-free operation under the specified service conditions. The maximum acceptable average piston speed
and the maximum acceptable rotating speed can be specified where experience indicates that specified limits should not be
exceeded for a given service.
Note: Generally, the rotating speed and piston speed of compressors in non-lubricated services should be less than those in equivalent lubricated
services.
6.5 ALLOWABLE DISCHARGE TEMPERATURE
6.5.1 Unless otherwise specified and agreed, the maximum predicted discharge temperature shall not exceed 150ºC (300ºF).
This limit applies to all specified operating and load conditions. The vendor shall provide the purchaser with both the predicted
and adiabatic discharge temperature rise.
Special consideration shall be given to services (such as high-pressure hydrogen or applications requiring non-lubricated
cylinders) where temperature limitations should be lower. Predicted discharge temperatures shall not exceed 135ºC (275ºF) for
hydrogen rich services (molar mass less than or equal to 12).
Commonly, compression ratios are higher in the first and second stages for full load. When the unit is unloaded by clearance
pockets in lower stages, the higher stages have the higher compression ratios. The discharge temperature should be reviewed at all
loading points.
Note: The adiabatic discharge temperature is the discharge temperature that would result from adiabatic compression. The actual discharge
temperature can differ from the adiabatic discharge temperature depending on such factors as the power input to a cylinder, the ratio of
compression, the size of the cylinder, the surface area of the cooling passages, and the velocity of the coolant. Non-lubricated hydrogen services
generally have higher discharge temperatures than lubricated hydrogen services because of slippage and the unusual characteristic of hydrogen,
which can release heat when it expands. With low power and small cylinders, the actual temperature rise can be lower than adiabatic
temperature, which can allow a lesser number of stages if the application is borderline. Conversely, large cylinders can result in a temperature
rise higher than adiabatic rise and can require additional stages.
• 6.5.2
A high discharge temperature alarm and shutdown device shall be provided for each compressor cylinder. When
specified, 100% unloading shall be furnished as part of the system by the supplier of these devices. The setpoints and the mode of
operation shall be mutually agreed upon by the purchaser and the compressor vendor.
The recommended discharge temperature alarm and trip setpoints are 20 K (40ºF) and 30 K (50ºF) respectively above the
maximum predicted discharge temperature; however, temperature trip setpoints shall not exceed 180ºC (350ºF). To prevent autoignition, lower temperature limits should be considered for air, due to oxygen content, if the discharge gauge pressure exceeds 20
bar (300 psig). Use of synthetic oils, although not intended as a means to increase the allowable discharge temperature, is
recommended for additional safety (see 6.14.3.1.9).
CAUTION: Oxygen bearing gases other than air require special consideration.
6.6 ROD AND GAS LOADS
6.6.1 The combined rod load shall not exceed the manufacturer’s maximum allowable continuous combined rod loading for the
compressor running gear at any specified operating load step. These combined rod loads shall be calculated on the basis of the setpoint pressure of the discharge relief valve of each stage and of the lowest specified suction pressure corresponding to each load
step.
6.6.2 The gas loading shall not exceed the manufacturer’s maximum allowable continuous gas loading for the compressor
static frame components (cylinders, heads, distance pieces, crosshead guides, crankcase, and bolting) at any specified operating
load step. These gas loads shall be calculated on the basis of the set-point pressure of the discharge relief valve of each stage and
of the lowest specified suction pressure corresponding to each load step.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
13
6.6.3 The combined rod loads and the gas loads shall be calculated for each 5-degree interval of one crankshaft revolution for
each specified load step on the basis of internal cylinder pressures using valve and gas passage losses and gas compressibility
factors corresponding to the internal cylinder pressure and temperature conditions at each crank angle increment. The internal
pressure during the suction stroke is the suction pressure at cylinder flange minus the valve and gas passage losses. The internal
pressure during the discharge stroke is the discharge pressure at cylinder flange plus the valve and gas passage losses.
6.6.4 For all specified operating load steps and the fully unloaded condition, the component of combined rod loading parallel to
the piston rod shall fully reverse between the crosshead pin and bushing during each complete revolution of the crankshaft. The
duration and magnitude of this reversal shall be consistent with the oil distribution design of the crosshead bushing in order to
maintain proper lubrication.
Note: Some bushing designs (such as grooved bushings) have proven reliability with as little as 15 degrees of rod reversal at 3% magnitude.
Simple bushing designs (un-grooved) may require a minimum of 45 degrees of rod reversal and a 20% magnitude. The manufacturer should
provide the actual requirements to the purchaser at the proposal stage.
6.6.5 The compressor shall be capable of handling short duration excursions of operation involving a load increase up to 10%
above the maximum allowable continuous combined rod load and/or maximum allowable continuous gas load. These excursions
shall be limited to a duration of less than 30 seconds and a frequency of no more than twice in a given 24-hour period.
6.7 CRITICAL SPEEDS
6.7.1 The compressor vendor shall perform the necessary lateral and torsional studies to demonstrate the elimination of any
lateral or torsional vibrations that may hinder the operation of the complete unit within the specified operating speed range in any
specified loading step. The vendor shall provide copies of the studies and shall inform the purchaser of all critical speeds from
zero to trip speed or synchronous speed that occur during acceleration or deceleration (see 9.2.3, Item r).
6.7.2 With the exception of belt driven units, the vendor shall provide a torsional analysis of all machines furnished. Torsional
natural frequencies of the complete driver-compressor system (including couplings and any gear unit) shall not be within 10% of
any operating shaft speed and within 5% of any multiple of operating shaft speed in the rotating system up to and including the
tenth multiple. For motor-driven compressors, torsional natural frequencies shall be separated from the first and second multiples
of the electrical power frequency by 10% and 5% respectively. For synchronous motor driven compressors, refer to the
requirements of 7.1.2.10.
6.7.3 For drive trains that include a turbine and gear, the requirements of ISO 10437, 13691, or API 611, 612, 613, 616, and
677, as applicable, shall govern in calculation and evaluation of critical speeds. For units requiring the use of a low-speed quill
shaft and coupling, a separate lateral critical speed analysis shall be performed. Any lateral critical speed of a quill shaft shall be
separated by at least 20% from any operating speed of any shaft in the system.
6.7.4 When torsional resonances are calculated to fall within the margin specified in 6.7.2, and the purchaser and the vendor
have agreed that all efforts to remove the critical from within the limiting frequency range have been exhausted, a stress analysis
shall be performed to demonstrate that the resonances have no adverse affect on the driver-compressor system. The assumptions
and acceptance criteria for this analysis shall be mutually agreed upon by the purchaser and the vendor.
6.8 COMPRESSOR CYLINDERS
6.8.1 General
6.8.1.1 The maximum allowable working pressure of the cylinder shall be at least equal to the specified relief valve set
pressure. If a set pressure is not specified, the maximum allowable working pressure of the cylinder shall exceed the maximum
stage discharge gauge pressure by at least 10% or 1.7 bar (25 psig), whichever is greater.
6.8.1.2 Unless otherwise specified, horizontal cylinders shall be used for compressing saturated gases or for gases carrying
injected flushing liquids. All horizontal cylinders shall have bottom discharge connections. Other cylinder arrangements may be
considered with the approval of the purchaser. In these cases, manufacturer shall provide the purchaser with an experience list for
similar services.
Note: Liquid in any form has detrimental effect on cylinder valve life and potentially on pressure packing and piston ring life. See notes at
7.7.1.4.
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API STANDARD 618
6.8.1.3 Cylinders shall be spaced and arranged to permit access for operating and removal for maintenance of all components
(including water jacket access covers, distance piece covers, packing, crossheads, pistons, valves, unloaders, or other controls
mounted on the cylinder) without removing the cylinder, the process piping, or pulsation suppressors.
6.8.1.4 Single acting, step piston, or tandem cylinder arrangements may be provided if accepted by the purchaser at the time of
purchase. For such cylinder arrangements, special consideration must be given to ensure rod load reversals (see 6.6.4.).
6.8.1.5 The walls of cylinders without liners (see 6.8.2.2) shall be thick enough to provide for reboring to a total of 3.0 mm
(1/8 in.) increase over the original diameter. The increase in piston diameter shall not affect the cylinder maximum allowable
working pressure, the maximum allowable continuous gas load, or the maximum allowable continuous combined rod load.
6.8.1.6 The use of tapped bolt holes in pressure parts shall be minimized. To prevent leakage in pressure sections of casings,
metal equal in thickness to at least half the nominal bolt diameter, in addition to the allowance for corrosion shall be left around
and below the bottom of drilled and tapped holes. The depth of the threaded holes shall be at least 1.5 times the stud diameter.
6.8.1.7 Bolting shall be furnished as specified in 6.2.
6.8.1.8 Cylinder heads, stuffing boxes for pressure packing, clearance pockets, and valve covers shall be fastened with studs.
The fastening configuration shall be designed so that these component parts can be removed without removing any studs. Torque
values for all studs and bolting shall be included in the manufacturer’s instruction manual.
CAUTION: Exceeding the manufacturer’s torque values on valve covers can cause damage to the valve assembly and cylinder
valve seat.
6.8.1.9 Studded connections shall be furnished with studs installed. Blind stud holes should only be drilled deep enough to
allow a preferred tap depth of 11/2 times the major diameter of the stud. The first 11/2 threads at both ends of each stud shall be
removed to allow the stud end to bottom in the hole. Class 4 and 5 fit studs shall be installed with a depth gauge and shall not
bottom in the holes. Anaerobic adhesive or similar epoxy bonding agents shall not be used with Class 1 or 2 fits.
6.8.1.10 Stud markings shall be located on the exposed end of the stud.
6.8.1.11 If extended studs are provided for hydraulic tensioning, the exposed threads shall be protected by a cover.
6.8.2 Cylinder Appurtenances
6.8.2.1 Cylinder supports shall be designed to avoid misalignment and resulting excessive rod runout during the warm-up
period and at actual operating temperature. The support shall not be attached to the outboard cylinder head, unless mutually
agreed upon by the purchaser and vendor. If head end cylinder supports are necessary, the design shall be such that misalignment
and/or excessive rod runout do not occur. The outboard cylinder support design shall be flexible in the direction of the piston rod
center line to allow for the thermal growth and axial stretch of the cylinder along this line). The pulsation suppressor shall not be
used to support the compressor cylinder.
6.8.2.2 Unless otherwise specified, each cylinder shall have a replaceable dry-type liner, not contacted by the coolant. Liners
shall be at least 9.5 mm (3/8 in.) thick for piston diameters up to and including 250 mm (10 in.). For piston diameters larger than
250 mm (10 in.), the minimum liner thickness shall be 12.5 mm (1/2 in.).
Liners shall be secured to prevent axial movement or rotation. The liner fit to the cylinder bore shall be designed to enhance heat
transfer and dimensional stability.
Note: Non-contacting vertical labyrinth type pistons do not necessarily need a replaceable liner.
6.8.2.3 The surface finish of the running bore of the cylinder liners and cylinders without liners used for applications with
metallic or nonmetallic wear bands and piston rings, for either lubricated or non-lubricated services, shall be 0.1 µm – 0.6 µm
(4 µin. – 24 µin.) Ra (arithmetic average roughness). The actual surface finish requirement is dependant on the choice of cylinder
liner material, coatings, operating conditions, and the degree of lubrication.
• 6.8.2.4
If specified, the running bore of cylinders with non-metallic, tetrafluoroethylene-based (TFE) rings shall be honed
using a hone surface of the same material as the rider bands and/or piston rings. The hone surface material and the method of
application shall be mutually agreed upon.
Note: Care should be taken during commissioning of cylinders, particularly non-lube cylinders, to monitor excessive early rider band wear
which can result in damage to the cylinder liner. After the initial run-in period, rider band wear normally decreases significantly.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
15
6.8.2.5 Where valve covers with radial captured o-rings are used, two extra-long studs 180 degrees apart shall be provided for
each cover to ensure the cover o-ring clears the cylinder valve-port bore before the valve cover clears the studs. Extra long studs
shall be capable of having a full-threaded nut when the o-ring is clear of cylinder valve-port sealing bore.
6.8.2.6 Valve cage designs shall be of the cylindrical type held in place by a circular contact cover. Center-bolt design shall not
be furnished (see Annex J for preferred approach). Designs that utilize three or more through bolts acting on the circumference of
the valve cage may be furnished with purchaser approval. If this design is furnished, the through bolts shall be self-retaining and
shall be furnished with cap type nuts and gaskets to prevent gas leakage.
6.8.2.7 The surface finish of valve port o-ring sealing surfaces shall not exceed an arithmetic average roughness Ra of 1.6 µm
(64 µin.). Valve ports using o-rings shall include an entering bevel for the o-ring.
6.8.2.8 Valve chambers and clearance pockets shall be designed to minimize trapping of liquid.
6.8.2.9 If drain connections are provided on external bottles used as clearance pockets, drain valves shall be provided (see 7.7.6
for piping material between clearance pocket and drain valve).
6.8.3 Cylinder Cooling
6.8.3.1 General
Cylinders shall have cooling provisions as required by the conditions of service described in 6.8.3.2 through 6.8.3.4.1 (see 7.7.4
and Figure G-1).
6.8.3.2 Static-filled Coolant Systems
Static-filled coolant systems (see Figure G-1, Plan A) may be supplied where cylinders are not required to operate fully unloaded
for extended periods of time, the expected maximum discharge temperature is less than 90°C (190°F), and the adiabatic gas
temperature rise (difference between suction temperature and discharge temperature based on isentropic compression) is less than
85K (150°F).
6.8.3.3 Atmospheric Thermosyphon Coolant Systems
Atmospheric thermosyphon coolant systems (see Figure G-1, Plan B) may be supplied when cylinders are not required to operate
fully unloaded for extended periods of time and either (a) the expected maximum discharge temperature is 100°C (210°F) or (b)
the adiabatic gas temperature rise is less than 85K (150ºF).
By mutual agreement between the purchaser and the vendor, a pressurized thermosyphon system may be used. The pressurized
system may only be used where the expected maximum gas discharge temperature is not to exceed 105°C (220°F). In such cases,
the system shall be supplied with a thermal relief valve set at a gauge pressure of 1.7 bar (25 psig) maximum.
6.8.3.4 Forced-liquid Coolant Systems
6.8.3.4.1 Forced-liquid coolant systems (see Figure G-1, Plan C) shall be provided when cylinders are operated while unloaded
for extended periods of time and either (a) the expected maximum discharge temperature is above 100°C (210°F) or (b) the
adiabatic gas temperature rise is 85K (150°F) or greater.
Note: For sites with ambient temperatures of 45ºC (110°F) or higher, thermosyphon or static-filled systems can be unsuitable. See 6.1.24 for
fully unloaded extended operation.
Non-cooled or air-cooled cylinders shall not be furnished except by mutual agreement of the purchaser and the vendor.
6.8.3.4.2 Forced-liquid coolant systems (see Figure G-1, Plan C) shall meet the requirements of 6.8.3.4.3 through 6.8.3.4.5.
6.8.3.4.3 The cylinder cooling system provided shall be adequate to prevent gas condensation. Coolant inlet temperature shall
be at least 5K (10ºF) above the inlet gas temperature. The coolant system shall be such that the above requirements are satisfied
under all operating and transient conditions including start-up from cold.
Note 1: Lower inlet coolant temperatures can cause condensation of gas constituents, which can be detrimental to the life of cylinder valves,
piston rings and packing.
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API STANDARD 618
Note 2: When the purchaser cannot supply coolant with adequate inlet temperature, a closed jacket cooling system compliant with 6.6.3.5, or an
inline heater as shown in Figure G-1, Plan C, should be considered.
Note 3: For most applications the inlet gas temperature is considered to be equal to the dew point. In applications where it is known that the gas
dew point is substantially below the gas inlet temperature and remains that way at all times during operation, a lower coolant inlet temperature
may be considered as long as condensation is avoided.
6.8.3.4.4 When possible, coolant exit temperatures should not be higher than 17K (30°F) above gas inlet temperature.
Note: Excessively high coolant exit temperatures can result in loss of capacity and efficiency.
6.8.3.4.5 Coolant flow and velocities should be sufficient to prevent solids suspended in the cooling media from depositing and
causing the fouling of jackets and passages.
6.8.3.5 Cooling Jacket Systems
6.8.3.5.1 The arrangement of the cooling jackets shall be such that failure of a gasket or other seal does not result in leakage of
coolant into the cylinder or gas into the cooling system. When cooling of cylinder heads is provided, separate non-interconnecting
jackets are required for cylinder bodies and cylinder heads.
• 6.8.3.5.2
If specified, a self-contained, forced circulation, closed jacket coolant system shall be furnished (see Figure G-1, Plan
D of Annex G). The coolant system shall meet the requirements of 6.8.3.4.3 and 6.8.3.4.5, as well as the requirements of 6.8.3.5.3
through 6.8.3.5.5.
6.8.3.5.3 A heating unit shall be provided as part of the self-contained closed jacket system for use during cold weather
operation and for bringing the system up to temperature before start-up.
6.8.3.5.4 The coolant circulated shall, if possible, be controlled to maintain a rise in coolant temperature across any individual
cylinder, including the cylinder heads if cooled, of between 5K (10ºF) and 10K (20ºF).
6.8.3.5.5 The system shall be pre-piped, factory skid mounted, and complete with the various pressure and temperature
indicators, alarms, and other instrumentation specified.
6.8.4 Cylinder Connections
6.8.4.1 General
6.8.4.1.1 All openings or nozzles for piping connections on cylinders shall be DN 20 (3/4 NPS) or larger and shall be in
accordance with ISO 6708. Sizes DN 32, DN 65, DN 90, DN 125, DN 175 and DN 225 (11/4 NPS, 21/2 NPS, 31/2 NPS, 5 NPS, 7
NPS, and 9 NPS) shall not be used.
6.8.4.1.2 All connections shall be flanged or machined and studded, except where threaded connections are permitted by
6.8.4.1.5. All connections shall be suitable for the maximum allowable working pressure of the cylinder as defined in 3.23.
Flanged connections may be integral with the cylinder or, for cylinders of weldable material, may be formed by a socket-welded
or butt-welded pipe nipple or transition piece, and shall terminate with a welding-neck or socket-weld flange.
6.8.4.1.3 Connections welded to the cylinder shall meet the material requirements of the cylinder, including impact values,
rather than the requirements of the connected piping (see 6.13.7.4). All welding of connections shall be completed before the
cylinder is hydrostatically tested (see 8.3.2).
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6.8.4.1.4 Butt-welded connections, size DN 40 (11/2 NPS) and smaller, shall be reinforced by using forged welding inserts or
gussets.
6.8.4.1.5 For connections other than main process connections, if flanged or machined and studded openings are impractical,
threaded connections for pipe sizes not exceeding DN 40 (11/2 NPT) may be used with purchaser’s approval in the following
cases:
a. on non-weldable materials, such as cast iron;
b. when essential for maintenance (disassembly and assembly).
6.8.4.1.6 Pipe nipples screwed or welded to the cylinder should be no more than 150 mm (6 in.) long and shall be a minimum
of Schedule 160 seamless for sizes DN 25 (1 NPS) and smaller and a minimum of Schedule 80 for DN 40 (11/2 NPS).
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
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6.8.4.1.7 The nipple and flange materials shall meet the requirements of 6.8.4.1.3.
6.8.4.1.8 Threaded openings and bosses for tapered pipe threads shall conform to ISO 7-1 and ISO 7-2 or ASME B16.5.
6.8.4.1.9 Threaded connections shall not be seal welded.
6.8.4.1.10 Threaded openings not to be connected to piping shall be plugged with solid, round-head steel plugs in accordance
with ASME B16.11. As a minimum, these plugs shall meet the material requirements of the pressure casing (or cylinder). Plugs
with the possibility of later removal shall be of a corrosion-resistant material. Plastic plugs shall not be used. A process
compatible thread lubricant of proper temperature specification shall be used on all threaded connections. Thread tape shall not be
used.
6.8.4.1.11 Machine and studded connections shall conform to the facing and drilling requirements of ISO 7005-1 or 7005-2 or
ASME B16.1, ASME B16.5, ASME B16.42, or ASME B16.47. Studs and nuts shall be furnished installed; the first 11/2 threads
at both ends of each stud shall be removed.
6.8.4.1.12 Machined and studded connections and flanges not in accordance with ISO 7005-1 or 7005-2 or ASME B16.1,
ASME B16.5, ASME B16.42, or ASME B16.47, except for non-circular cylinder connections described in 6.8.4.2.1, shall be
approved by the purchaser. Unless otherwise specified, the vendor shall supply mating flanges, studs, and nuts for these nonstandard connections.
6.8.4.1.13 To minimize nozzle loading and facilitate installation of piping, each main flange shall be parallel to the plane
shown on the general arrangement drawing to within 0.5 degrees. Studs or bolt holes shall straddle centerlines parallel to the main
axes of the equipment.
Note: For piping installation requirements see API 686 (see 6.3.3).
6.8.4.1.14 All of the purchaser’s connections shall be accessible for disassembly without requiring the machine, or any major
part of the machine, to be moved.
6.8.4.1.15 The finish of the gasket contact surfaces of cast iron, ductile iron, or steel connections (flanged or machined bosses),
other than ring-type joints or non-circular joints, shall be between 3.2 µm and 6.4 µm (125 µin. and 250 µin.) arithmetic average
roughness (Ra). Either a serrated-concentric finish or a serrated-spiral finish having 0.6 mm – 1.0 mm pitch (24 – 40 grooves per
in.) shall be used. The surface finish of the gasket grooves of ring joint connections shall conform to ISO 7005-1 or ISO 7005-2 or
ASME B16.5.
• 6.8.4.1.16
If specified, each cylinder shall be provided with a DN 12 (NPT 1/2) indicator tap at each end. Designs similar to
Figure G-2, with a corrosion-resistant sleeve arrangement inside a continuous cast-in membrane to provide a positive gas-tight
seal, are acceptable for cast iron and nodular iron cylinders. Materials shall be compatible with the gas.
• 6.8.4.1.17
If specified, indicator valves shall also be provided. If indicator valves are not furnished, the tapped indicator holes
shall be plugged in accordance with 6.8.4.1.10.
6.8.4.2 Flanges
6.8.4.2.1 Flanges shall conform to ISO 7005-1 or 7005-2 or ASME B16.1, B16.5, B16.42 or B16.47 Series B as applicable,
except as specified in 6.8.4.2.2 through 6.8.4.2.7 (see 6.8.4.1.15 for facing finish requirements). The details of any special
connections, such as a lens joint, shall be submitted to the purchaser for review (see Annex F). For low-pressure cylinders, where
noncircular connections are used, the vendor shall supply inlet and discharge transition pieces with the termination flange
consistent with the agreed flange standards. The transition pieces shall be of the same grade of material as, or of a higher grade of
material than the cylinder. The vendor shall supply all gaskets, studs, and nuts between the cylinder and transition piece.
6.8.4.2.2 Cast iron flanges shall be flat faced and conform to the dimensional requirements of ISO 7005-2 or ASME B16.1 or
l6.42. Class 125 flanges shall have a minimum thickness equal to Class 250 for sizes DN 200 (8 NPS) and smaller.
6.8.4.2.3 Steel flanges shall conform to the dimensional requirements of IS0 7005-1, ASME B16.5 or ASME B16.47.
6.8.4.2.4 Non-ferrous flanges shall conform to mutually agreed upon standards such as ISO 7005-3.
6.8.4.2.5 Flat-face flanges with full raised face thickness are permitted on cylinders of all materials. Flanges in all materials
that are thicker or have a larger outside diameter than required by the applicable flange standards are permitted. The dimensions
of non-standard (oversized) flanges shall be shown on the arrangement drawing in full detail.
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API STANDARD 618
Note: Flat-faced flanges, in lieu of recessed or female face flanges, are typically needed to permit removal of the cylinder without removing or
springing piping or pulsation dampeners. Ring type joints (RTJ) and lens type joints should be discussed between the purchaser and vendor on a
special requirement basis.
6.8.4.2.6 Flanges shall be full faced or spot faced on the back and shall be designed for through bolting.
6.8.4.2.7 The flange gasket contact surface shall not have mechanical damage that penetrates the root of the grooves for a
radial length of more than 30% of the gasket contact width.
6.8.5 External Forces and Moments
The vendor shall define the maximum allowable nozzle loads at the vendor interfaces. These loads shall be referred to a
coordinate system as shown on a drawing.
6.9 VALVES AND UNLOADERS
6.9.1 Valves
6.9.1.1 Average valve gas velocity shall be calculated as shown in Equation 1:
In SI units
W = F × cm ⁄ f
(1)
where
W
is the average gas velocity in m/s;
F
is the effective piston area of the cylinder end or ends concerned. For a double acting cylinder, this is the area of the
crank-end of the cylinder less the piston rod plus the area of the outer end of the piston in cm2;
ƒ
is the product of the actual lift, the valve-opening periphery, and the number of inlet or discharge valves in cm2;
cm
is the average piston speed in m/s.
In USC units
V = 288 × D ⁄ A
where
V
is the average gas velocity in ft/min;
D
is the piston displacement per cylinder in ft2/min;
A
is the product of the actual lift, the valve-opening periphery, and the number of inlet or discharge valves per cylinder
in in.2.
The valve lift used in Equation 1 shall be shown on the data sheets.
If the lift area is not the smallest area in the flow path of the valve, that condition shall be noted on the data sheet and the velocity
shall be computed on the basis of the smallest area. Velocities calculated from Equation 1 should be treated only as a general
indication of valve performance and should not be confused with effective velocities based on crank angle, degree of valve lift,
unsteady flow, and other factors. The velocity computed from Equation 1 is not necessarily a representative index for valve power
loss or disk/plate impact.
6.9.1.2 Valve and unloader designs shall be suitable for operation with all gases specified. Each individual unloading device
shall be provided with a visual indication of its position and its load condition (loaded or unloaded).
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19
6.9.1.3 The valve design, including that for double-decked valves, shall be such that valve assemblies cannot be inadvertently
interchanged or reversed. For example, it shall not be possible to fit a suction valve assembly into a discharge port, nor a discharge
valve assembly into a suction port; nor shall it be possible to insert a valve assembly upside down.
6.9.1.4 Valve assemblies (seat and guard) shall be removable for maintenance. Valve-seat-to-cylinder gaskets shall be solid
metal or metal jacketed. Valve-cover-to-cylinder gaskets shall be either solid metal, the flexible graphite type, metal jacketed, or
the o-ring type. Other gasket types may be used with mutual agreement between the purchaser and the vendor.
Note: Flexible graphite-type gaskets with a suitable reinforcement have been successfully used to seal valve cover to cylinder gaskets where low
mole weight gases are compressed.
6.9.1.5 The valve and cylinder designs shall be such that neither the valve guard nor the assembly bolting can fall into the
cylinder even if the valve assembly bolting breaks or unfastens.
6.9.1.6 When discharge valve assemblies, including any cage or chair, have a mass of 15 kg (35 lb) or more, the vendor shall
provide a device to facilitate removal and installation of valve assemblies for maintenance. On all under-slung valves, an
arrangement shall be provided to hold the complete valve assembly in position while the cover is installed.
6.9.1.7 The ends of coil-type valve springs shall be squared and ground to protect the plate against damage from the spring
ends.
6.9.1.8 Valve hold-downs shall bear at not less than three points on the valve assembly. The bearing points shall be arranged as
symmetrically as possible (see 6.8.2.6).
• 6.9.1.9
The vendor shall conduct a computer study of the valve dynamics to optimize the valve sealing element motion during
the opening and closing phase. The mathematical models being used for the valve motion calculation shall, as a minimum, take
into account: valve sealing element masses, spring forces, aerodynamic drag coefficients, fluid damping, and any other factors
deemed necessary by the vendor to assess valve element motion, impact, and efficiency. The study shall also include a valve
dynamic response analysis of the valve component’s reactions to the piping and compressor cylinder gas passage induced
pulsations. The study shall include a review of all operating gas densities and load conditions.
If specified, the vendor shall submit a written valve dynamics report to the purchaser.
6.9.1.10 Metal valve disks or plates, when furnished, shall be suitable for installation with either side sealing and shall be
finished on both sides to an Ra of 0.4 µm (16 µin.) or better. Edges shall be suitably finished to remove stress risers. Valve seats
and sealing surfaces shall also be finished to an Ra of 0.4 µm (16 µin.) or better. When non-metallic valve plates or disks are
furnished, flatness and surface finish shall be controlled so that adequate sealing occurs in operation. The vendor shall provide the
properties of non-metallic valve plate materials. These properties shall include filler type and content, specific gravity, melting
temperature, glass transition temperature (where applicable), izod impact strength (notched and un-notched), water absorption
and coefficient of thermal expansion. Reinforcement of non-metallic materials shall be with fibers, not with spherical beads or
other shapes. Fibers shall be oriented to optimize component life (e.g., the fibers shall follow the stress path).
6.9.2 Unloaders
• 6.9.2.1
If cylinder valve unloading is specified, the type of unloader provided (valve depressor or plug-type) shall be mutually
agreed upon. Valve assembly lifters shall not be used. When valve depressors are used for capacity control, all inlet valves of the
cylinder end involved shall be so equipped where possible. Use of less than a full complement of suction valve depressors
requires the purchaser’s approval.
6.9.2.2 Where plug-type unloaders are used for capacity control, the number of unloaders is determined by the area per plug
opening, the total of which must be equal to or greater than half of the total free lift area (or least flow area) of all suction valves
on that end. The unloader assembly shall positively guide the plug to the seat.
6.9.2.3 When valve depressors are used only for start-up and never for capacity control, consideration shall be given to using a
reduced number of unloaders. For start-up with plug unloaders, only one per cylinder end is needed.
• 6.9.2.4
Unloaders shall be pneumatically or hydraulically actuated. Individual hand-operated unloaders or manual overrides on
actuated unloaders are not permitted. Remotely controlled unloaders shall be designed by the vendor in such a manner that the
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Note: Special precautions may be necessary when using valve plate depressors in combination with non-metallic valve plates or discs. Special
precautions are also necessary when using non-metallic valve plate depressors, with respect to unloaded or alternate conditions, which may
cause higher operating temperatures.
20
API STANDARD 618
correct sequence of operation between stages and cylinder ends is achieved. The vendor shall provide the user with information
regarding the proper sequencing for unloader operation. See 7.6.2.4.
Note: Malfunctioning and/or incorrect sequencing of unloaders can result in overload or unbalance of the compressor.
6.9.2.5 For turbine driven, geared applications, cylinder unloaders shall be provided on each cylinder end for emergency
shutdown.
6.9.2.6 Unloaders shall be designed so that the operating fluid used for unloading cannot mix with the gases being compressed,
even in the event of failure of the diaphragm or another sealing component. A threaded gas vent connection shall be provided at
the stem packing.
Unloader sliding push rods exposed to atmospheric conditions shall be of corrosion-resistant material.
6.9.2.7 If specified, a stainless steel protective sheet metal rain shield shall be furnished to protect exposed topside unloader
parts from the elements. The rain shield shall be fabricated with a handle for easy removal and replacement. See Annex J for a
sketch of the rain cover.
Note: Moisture can gather around the seals on the top of exposed unloaders and mix with airborne elements to form a corrosive mixture. The
mixture can etch unloader shafts and lead to premature unloader failure, which can be erroneously contributed to moisture-laden control gas.
6.10 PISTONS, PISTON RODS, AND PISTON RINGS
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6.10.1 Connection of Piston-to-piston Rod
Pistons that are removable from the rod shall be attached to the rod by a shoulder and nut(s) design or a multi-through-bolt design.
Other proven attachment methods may be used, and in such cases they shall be noted in the proposal. Mechanical or hydraulic
methods are acceptable for tightening piston nuts. Slugging (hammer) wrenches shall not be used for this procedure.
As a basic requirement, the manufacturer’s tightening procedure shall assure a minimum pre-load in the connection of 1.5 times
the maximum allowable continuous rod loading (see Figure G-9).
6.10.2 Connection of Piston Rod to Crosshead
6.10.2.1 Piston rods shall be connected to the crosshead by (a) a direct connection, where the rod is threaded into the crosshead
(e.g. jambnut design, or a multi-bolt design) (e.g., Figure G-6), or (b) an indirect connection, where the rod is not threaded into the
crosshead (e.g., see Figures G-7 and G-8) (see Tightening Diagram Figure G-9). Positive locking of the rod shall be provided for
direct connection methods.
Other proven attachment methods (e.g., Figure G-8) may be used, and in such cases they shall be noted in the proposal.
Mechanical or hydraulic methods are acceptable for tightening. Slugging wrenches for this procedure shall not be used. Where
pre-load is achieved by hydraulic tensioning methods, which ensure the proper pre-load, positive locking is not required.
6.10.2.2 The manufacturer’s tightening procedure shall assure a minimum preload in the connection equal to 1.5 times the
maximum allowable continuous rod loading (see Figure G-9).
Note: The process for attaching the piston rod to the piston and to the crosshead should be performed in accordance with the manufacturer’s
standard.
6.10.3 Pistons
6.10.3.1 Hollow pistons (single piece or multi-piece) shall be continuously self-venting; i.e., they shall depressure when the
cylinder is depressured. Acceptable methods of venting include a hole located in the head-end face of the piston in the form of a
single hole 3 mm (1/8 in.) in diameter, a hole at the bottom of the piston ring groove, or a spring-loaded relief plug in the outer-end
face of the piston.
• 6.10.3.2
If specified, wear bands shall be of single- or multi-piece construction designed to prevent underside pressurization
(acting similarly to a piston ring). If feasible, pistons shall be segmented to facilitate wear band installation. Piston ring carriers
supplied with multi-piece pistons shall be made of wear resistant material. Nonmetallic wear bands shall not overrun fully open
single-hole valve ports or liner counter-bores by more than half the width of the wear band. When the cylinder configuration leads
the wear band to overrun the valve ports by more than half the band width, the port design shall be of the multiple-drilled-hole
type to provide sufficient support for the wear band.
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21
For non-lubricated, horizontal cylinders, the bearing load calculated from Equation 2 on nonmetallic wear bands shall not exceed
0.035 N/mm2 (5 lbf/in.2) based on the mass of the entire piston assembly plus half the mass of the rod divided by the projected
area of a 120º arc of all wear bands (see Equation 2).
For lubricated horizontal cylinders, the bearing load calculated from Equation 2 on wear bands, if used, shall not exceed 0.07 N/
mm2 (10.0 lbf/in.2) using the same approach described for nonmetallic wear bands.
M PA + ( M R ⁄ 2 )
L B = -------------------------------------(2)
( 0.866 × D × W )
where
LB
MPA
MR
is the bearing load on wear band in N/mm2 (lbf/in.2);
is the weight of piston assembly in N (lbf);
is the weight of piston rod in N (lbf);
D
is the cylinder bore diameter in mm (in.);
W
is the total width of all wear bands in mm (in.).
Note: When meeting the bearing load requirement results in an excessively wide wear band, multiple wear bands are preferred.
6.10.4 Piston Rods
6.10.4.1 Unless otherwise specified, all piston rods, regardless of base material, shall be coated with a wear resistant material.
The material and surface treatment of piston rods shall be chosen to maximize rod and pressure packing life and shall be proposed
by the vendor at the time of purchase for the purchaser’s acceptance. Coatings shall comply with 6.10.4.2. Piston rod base
material and coatings for use in corrosive environments shall be suitable for the service and operating conditions specified.
6.10.4.2 When coatings are used, piston rods shall be continuously coated from the piston rod packing through the oil wiper
travel areas. The coating material must be properly sealed to prevent corrosion of the base material at the interface of the coating.
Fusion techniques that require temperatures high enough to permanently affect the mechanical characteristics of the base material
shall not be used. High-velocity and high-impact thermal coating processes are acceptable for the coating of piston rods. Metal
spray techniques requiring roughening of the surface of the base metal are not recommended because of the potentially
destructive stress risers left in the surface. Use of sub-coating under the main coating is not recommended.
Note: Piston rods that have been previously induction-hardened should not be coated with a wear resistant material over the induction-hardened
case.
6.10.4.3 The base material of piston rods used in H2S service shall be in accordance with NACE MR0175 (see 6.15.1.11).
When this requirement results in insufficient surface hardness for wear resistance, a proven surface treatment or coating shall be
proposed for purchaser’s approval.
6.10.4.4 Tolerances for finished rods shall be 12.5 µm (0.0005 in.) for roundness and 25 µm (0.001 in.) for diametral variation
over the length of the rod.
The surface finish in the packing areas for lubricated and non-lubricated services shall be 0.15 µm to 0.4 µm (6 µin. – 16 µin.) Ra.
Note: Smoother finishes should be considered for high pressures or for particular material combinations where experience indicates that such
finishes can result in improved performance.
6.10.4.5 Piston rods with threads shall be furnished with rolled threads having a polished thread relief area. The vendor shall
state in the proposal the rod material and type of connection (see Figures G-6, G-7 or G-8). If NACE-MR0175 must be applied
because of H2S gas service (as defined in 6.13.1.11), the rod material will be considered acceptable as long as the base hardness
and yield strength remain within the specified NACE values. An increase in hardness around thread surface due to thread rolling
is acceptable as long as the base hardness meets NACE requirements.
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Alternatively, an uncoated piston rod may be proposed when the expected life equals or exceeds that of a coated rod for the
specified operating conditions. Uncoated piston rods shall be AISI 4140 or better and shall be surface hardened in the packing
area to a hardness of at least Rockwell C 50, and shall be inspected for cracking by magnetic particle examination.
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API STANDARD 618
6.10.4.6 Tail rods shall be used only with purchaser’s written approval. When tail rods are deemed acceptable, tail rod packing
assemblies shall be equal in design and quality to packing assemblies for piston rods. Tail rod surface treatment and finish shall be
the same as for the piston rod. Tail rod design shall include a device to positively prevent the tail rod from being ejected in the
event that it becomes disconnected from the piston/piston rod. Rod runout measured at the tail rod packing assembly shall not
exceed the limits defined in 6.3.1.
6.11 CRANKCASES, CRANKSHAFTS, CONNECTING RODS, BEARINGS AND CROSSHEADS
6.11.1 Crankshafts
For compressors above 150 kW (200 hp), crankshafts shall be forged in one piece and shall be heat-treated and machined on all
working surfaces and fits. The use of removable counterweights is acceptable. For compressors equal to or less than 150 kW
(200 hp), ductile iron is acceptable for crankshafts. The crankshafts shall be free of sharp corners. Main and crankpin journals
shall be ground to size. Drilled holes or changes in section shall be finished with generous radii and shall be highly polished.
Forced lubrication passages in crankshafts shall be drilled. See 8.2.2.3.3 for ultrasonic testing of crankshafts.
6.11.2 Bearings
6.11.2.1 For compressors above 150 kW (200 hp), replaceable, precision-bored shell (sleeve) crankpin bearings and main
bearings shall be used. For compressors equal to or less than 150 kW (200 hp), tapered roller type bearings are acceptable for
main bearings. Cylindrical, roller, or ball type bearings may be used only with the purchaser’s approval.
Note: Purchasers should recognize that the use of rolling element bearings can affect the service life of the compressor.
6.11.2.2 When rolling element bearings are allowed, they shall be supplied in compliance with 6.11.2.3 and 6.11.2.4.
6.11.2.3 All rolling element bearings shall be suitable for belt drive applications and shall give an L10-rated life, calculated in
accordance with ISO 281-1 or AFBMA 11, of either 50,000 hours with continuous operation at rated conditions or 25,000 hours
at maximum axial and radial loads and rated speed. (The rating life is the number of hours at rated bearing load and speed that
90% of the group of identical bearings will complete or exceed before the first evidence of failure.)
6.11.2.4 Rolling element bearings shall be secured to the shaft by a shrink fit and fitted into housings in accordance with the
applicable AFBMA recommendations.
6.11.3 Connecting Rods
For compressors above 150 kW (200 hp), connecting rods shall be forged steel with removable caps. For compressors equal
to or less than 150 kW (200 hp), ductile iron, steel plate, or cast steel connecting rods are acceptable. The connecting rods
shall be free of sharp corners. Forced lubrication passages shall be drilled. Drilled holes or changes in section shall be
finished with generous radii and shall be highly polished. Crankpin bushings shall be of the replaceable precision-bored
type and shall be securely locked in place. All connecting rod bolts and nuts shall be securely locked with cotter pins or
wire after assembly. Connecting rod bolts shall have rolled threads.
6.11.4 Crossheads
For compressors above 150 kW (200 hp), crossheads shall be made of steel. For compressors equal to or less than 150 kW
(200 hp), ductile iron is acceptable for crossheads. The crosshead top and bottom shoes or guides shall be replaceable. Facilities
shall be provided for the adjustment of crosshead clearance and alignment. Field machining for adjustment of clearances shall be
avoided. Adequate openings shall be provided to service crosshead assemblies.
6.11.5 Crankcases
• If specified, the crankcase shall be provided with relief devices to protect against rapid pressure rise. These devices shall
incorporate downward-directed apertures (away from the operator’s face), a flame-arresting mechanism, and a rapid closure
device to minimize reverse flow. The ratio of the total throat area of these devices to the crankcase free volume should be
no less than 70 mm2/dm3 (3 in.2/ft3).
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When not an integral part of the frame, crosshead housings shall be attached to the crankcase with studs. A metal-to-metal joint,
prepared with suitable sealant, shall be used between the crosshead housing and crankcase, the crosshead housing and distance
piece, and the distance piece and cylinder.
6.12 DISTANCE PIECES
6.12.1 Distance Piece Types
• 6.12.1.1
The purchaser shall specify the type of distance piece to be supplied. The types are listed in 6.12.1.2 through 6.12.1.5
(see Figure G-3).
6.12.1.2 Type A—short, single-compartment distance piece used only for lubricated service when oil carry-over (at the wiper
packing and cylinder pressure packing) is acceptable. In this application, part of the piston rod may alternately enter the
crankcase (crosshead housing) and the gas cylinder pressure packing. This arrangement shall not be used when cylinders are
lubricated with synthetic oils (see 6.14.3.1.9).
Note: Type A distance pieces are used only for nonflammable or non-hazardous gases.
6.12.1.3 Type B—long single-compartment distance piece used for non-lubricated service or for lubricated service where oil
carryover is not acceptable. No part of the piston rod shall alternately enter the crankcase (crosshead housing) and the gas
cylinder pressure packing. The rod shall be fitted with an oil slinger of spark resistant material and preferably of a split design for
easy access to the packing.
• 6.12.1.4
Type C—long/long two-compartment distance piece designed to contain flammable, hazardous, or toxic gases. No
part of the piston rod shall alternately enter the wiper packing, intermediate partition packing, and the cylinder pressure packing.
Segmental packing shall be provided between the two compartments. If necessary, provisions for lubrication of the segmental
packing shall be furnished by the vendor. If specified, provisions for the injection of buffer gas shall also be provided.
Note: The Type C distance piece with two oil slingers, one in each compartment, is not normally used on process compressors. This type of
distance piece is used only for special services such as oxygen service. This distance piece design causes the overall length of the gas end
assembly to become excessively large, thus causing the overall width of the compressors to become large, and therefore increasing foundation
requirements. Uses of such distance pieces can cause piston-rod diameters to increase because of the column effect of excessively long piston
rods.
Type D—long/short two-compartment distance piece designed to contain flammable, hazardous, or toxic gases. No
• 6.12.1.5
part of the piston rod shall alternately enter the wiper packing and the intermediate partition packing. Segmental packing shall be
provided between the two compartments. Provisions for lubrication of this segmental packing, if necessary, and, if specified, for
the injection of buffer gas shall be furnished by the vendor.
Note: The buffer gas should be a non-flammable, non-reactive or inert gas such as nitrogen.
6.12.2 Distance Piece Requirements
• 6.12.2.1
Access openings of adequate size shall be provided in all distance pieces to permit removal of the assembled packing
case. On Type D, two-compartment distance pieces, the compartment adjacent to the cylinder (the outboard compartment) may be
accessible through a removable partition. Distance pieces (or compartments) shall be equipped with screened safety guards,
louvered weather covers, or gasketed solid metal covers as specified.
All access openings shall be surfaced and drilled to accommodate solid metal covers. Nonmetallic covers are not permitted.
6.12.2.2 Distance piece design shall be such that the packing rings can be removed and replaced without removal of the piston
rod.
Note: In the case of small compressors, it can be easier to remove the piston rod.
• 6.12.2.3
Where solid metal distance piece covers are provided or specified, the distance piece, partitions, covers, bolting, and
the intermediate partition packing shall be designed for a minimum compartment differential pressure of 2 bar (25 psi) or higher,
if specified. The vendor shall indicate the maximum allowable working pressure (MAWP) of the distance piece. The purchaser
shall specify the maximum allowable back pressure on the vent system.
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24
API STANDARD 618
• 6.12.2.4
Each distance piece compartment shall be provided with the following connections:
a. top vent connection at least DN 40 (NPT 11/2);
b. bottom drain connection;
c. if specified, a purge or vacuum connection;
d. a packing vent connection below the rod to facilitate liquid draining of the packing case;
e. when required, packing lubrication;
f. where packing case cooling is required or specified, inlet and outlet connections on the distance piece suitably arranged to
facilitate draining and venting.
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See Figure G-3. See Annex I for vent and purge system schematics. Closed, sealed, or purged distance pieces not utilizing the DN
40 (NPT 11/2) free vent connection shall be equipped with a relief device having an area at least equal to the area of the hole
through the crank-end-head piston-rod hole minus the area of the piston rod. The vendor shall confirm that the DN 40 (NPT 11/2)
free vent connection or relief device is adequate to prevent overpressure of the distance piece in the event of a packing case
failure.
6.12.2.5 All external connections, except the top vent, shall be at least DN 25 (NPT 1).
6.12.2.6 Distance piece compartments with internal reinforcing ribs shall have internal drain provisions through the ribs.
6.12.2.7 Internal packing vent tubing and fittings shall be of austenitic stainless steel.
6.12.2.8 Unless otherwise specified, all external drain, vent, and purge piping and equipment shall be provided by the
purchaser.
6.12.2.9 For Type A and B distance pieces with solid metal covers, positive seal rings shall be provided at the wiper packing.
For Types C and D distance pieces with solid metal covers, positive seal rings shall be provided at both the wiper packing and the
intermediate partition packing. These seal rings shall be of the segmental type that effectively seal at atmospheric pressure
(without purge) to prevent contamination of the crankcase oil by leakage from the cylinder pressure packing (see 6.13.1.6).
6.13 PACKING CASES AND PRESSURE PACKING
6.13.1 General
• 6.13.1.1
All oil-wiper packing, intermediate partition packing, and cylinder pressure packing, shall be segmental rings with
garter springs of a nickel chromium alloy (such as Inconel 600 or X750). If specified, shields shall be provided in the crosshead
housings over the oil return drains from the wiper-packing stuffing boxes to prevent splash flooding.
6.13.1.2 Packing case flanges shall be bolted to the cylinder head or to the cylinder with no less than four bolts. Flanges shall
be of steel for flammable, hazardous, or toxic gas service. Packing cases shall be pressure rated at least to the maximum allowable
working pressure (MAWP) of the cylinder. Packing case assemblies shall have positive alignment features, such as cup-to-cup
pilot fits and/or sufficient body-fitted tie bolts.
6.13.1.3 For flammable, hazardous, toxic, or wet gas service, the pressure packing case shall be provided with a common vent
and drain, below the piston rod, piped by the vendor to the lower portion of the distance piece. See Annex G.
6.13.1.4 Adequate radial clearance shall be provided between the piston rod and all adjacent stationary components to prevent
contact when the maximum allowable wear occurs on the piston wear bands.
6.13.1.5 Crosshead packing boxes shall employ wiper packing to effectively minimize oil leakage from the crankcase.
• 6.13.1.6
If specified, to reduce process gas emissions to an absolute minimum, the cylinder pressure packing shall include
venting and buffer gas cups with side-loaded packing rings in the adjacent sealing cups. See the arrangement in Figure I-3.
Note: The buffer gas should be a non-flammable, non-reactive or inert gas such as nitrogen.
6.13.1.7 Unless otherwise specified, the manufacturer shall provide suitable devices and instructions to enable the piston rod to
be passed through the completely assembled cylinder pressure packing without damage.
Note: There is a risk of packing damage when using entering sleeves. However, when the outside diameter of the entering sleeve is equal to the
outside diameter of the rod, the risk is reduced when the manufacturer’s instructions are followed.
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6.13.2 Pressure Packing Case Cooling Systems
6.13.2.1 Unless otherwise specified, the criteria given in 6.13.2.2 through 6.13.2.6 shall be followed for the cooling of pressure
packing cases.
6.13.2.2 The manufacturer’s standard design may be used for cylinder discharge gauge pressure to 100 bar (1500 psig).
6.13.2.3 Packing cases shall be designed for liquid cooling with totally enclosed cooled cups for the following applications:
a. all non-lubricated packing rings;
b. lubricated non-metallic rings, when the cylinder maximum allowable working pressure (MAWP) is above 35 bar (500 psig);
c. all materials, lubricated or non-lubricated, when the cylinder maximum allowable working pressure (MAWP) is above 100 bar
(1500 psig).
6.13.2.4 When liquid cooled packing cases are furnished:
a. o-rings shall be used to seal coolant passages between cups;
b. o-rings shall be fully captured in grooves, both on the inside and outside diameter of the o-ring. A small relief recess of 0.5 mm
– 1 mm (0.015 in. – 0.030 in.) shall be provided around the captured o-ring to detect gas leakage. O-rings that encircle the piston
rod are not allowed; and
c. cases are to be tested for leakage on the coolant side to a gauge pressure not less than 8 bar (115 psig).
6.13.2.5 Cooling of pressure packing is not required for non-lubricated cylinders having a maximum allowable working
pressure (MAWP) below 17 bar (250 psig). Coolant connections in the packing cases shall be plugged with threaded steel plugs.
6.13.2.6 When the packing case is cooled by forced circulation, the vendor shall supply internal tubing and forged fittings of
austenitic stainless steel. A suitable filter having a 125 µm (125 microns) nominal rating or better and located external to the
distance piece shall be provided. If external tubing is provided by the vendor, it shall be austenitic stainless steel.
• 6.13.2.7
When cooling of cylinder pressure packing is required, the vendor shall be responsible for determining and informing
the purchaser of minimum requirements such as flow, pressure, pressure drop, and temperature, as well as any filtration and
corrosion protection criteria. The coolant pressure drop through the packing case shall not exceed 1.7 bar (25 psig).
If specified, the vendor shall supply a closed liquid cooling system. If specified, and for all sour or toxic gas services, this system
shall be separate from the cylinder jacket cooling system. See Figure G-4 for additional details on self-contained cooling systems
for cylinder pressure packing.
Note: The inlet packing case coolant temperature should not exceed 35ºC (95ºF). Packing efficiency increases with low coolant temperature.
6.14 LUBRICATION
6.14.1 General
In addition to the requirements of ISO 10438-1 and ISO 10438-3 or API 614, Chapters 1 and 3, the following requirements apply
to compressor lube oil systems:
6.14.2 Compressor Frame Lubrication
6.14.2.1.1 For compressors 150 kW (200 hp) and above, the frame lubrication system shall be a pressurized system. Splash
lubrication systems may be used on horizontal compressors of 150 kW (200 hp), or less, with rolling element bearings. The
crankcase oil temperature shall not exceed 70ºC (160ºF) for pressurized oil systems and 80ºC (180ºF) for splash systems. Cooling
coils shall not be used in crankcases or oil reservoirs.
6.14.2.1.2 Unless otherwise specified, pressure lubrication systems shall be general-purpose systems designed and furnished in
accordance with ISO 10438-1 and ISO 10438-3 or API 614, Chapters 1 and 3, except as modified below.
• 6.14.2.1.3
If specified, pressure lubrication systems shall be special-purpose systems designed and furnished in accordance
with ISO 10438-1 and ISO 10438-2, or API 614, Chapters 1 and 2.
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6.14.2.1 General
26
API STANDARD 618
Note: Special-purpose systems in accordance with ISO 10438-2 or API 614, Chapter 2, are typically applied only to reciprocating compressor
trains involving a large turbine driver and gear unit.
a. reservoir—typically the compressor crankcase;
b. main oil pump—(materials in accordance with 6.14.2.1.5) which may be shaft-driven or motor driven;
c. auxiliary pump, when required, in accordance with 6.14.2.2;
d. single cooler (see 6.14.2.3);
e. dual filters (see 6.14.2.4);
f. heater—when required (see 6.14.2.5);
g. pressure relief valve for each pump (see 6.14.2.6);
h. single regulator for control of delivered oil pressure (separate from relief valves);
i. single regulator for oil temperature control (see 6.14.2.7);
j. valves—material shall be carbon steel with stainless steel trim;
k. oil piping—shall be stainless steel pipe and fittings (with the exception of cast-in-frame lines or passages); or stainless steel
tubing and fittings (see 6.14.2.1.8);
l. The following instruments:
—
—
—
—
—
—
—
one pressure indicator;
two temperature indicators;
one level indicator (on the crankcase or reservoir) (see 6.14.2.1.9);
one pressure transmitter for low pressure alarm and auxiliary pump start;
one low frame oil level transmitter for alarm;
one filter high differential pressure transmitter for alarm;
one pressure transmitter for low pressure shutdown.
See Figure G-5 for a typical schematic drawing of a lube-oil system.
6.14.2.1.5 All external oil-containing pressure components, including auxiliary pumps, shall be steel; except that crankshaftdriven lube-oil pumps may have cast iron or nodular iron casings.
6.14.2.1.6 The rated gauge pressure of the frame lubrication system shall be not less than 10 bar (150 psig) (this is a system
design criterion only, the manufacturer’s recommended bearing supply pressure may be significantly less). The relief valve
setting shall be no greater than the sum of the normal bearing supply pressure, the equipment and piping pressure losses upstream
of the filter, and the cartridge collapsing differential pressure drop at a minimum oil temperature of 27ºC (80ºF) at the normal flow
rate to the bearings.
6.14.2.1.7 To prevent the oil from being contaminated if the cooler fails, the oil-side operating pressure shall be higher than the
water-side operating pressure.
6.14.2.1.8 Lap-joint or slip-on flanges are not allowed.
6.14.2.1.9 The oil reservoir shall be equipped with an oil-level sight glass. The maximum and minimum operating levels shall
be permanently indicated.
• 6.14.2.1.10 If specified, the oil system shall be run in the vendor’s shop and inspected in accordance with 8.2.3.2.
• 6.14.2.2 Auxiliary Pump
For each unit having a nominal frame rating of more than 150 kW (200 hp), the vendor shall provide a separate, independently
driven, full-capacity, full pressure auxiliary oil pump with an automatic start feature activated by low lube oil pressure and include
provisions for post-lubrication after shutdown.
The vendor shall supply the type of driver specified. Unless otherwise specified, pump drivers shall be sized for the pump power
and required starting torque at an oil kinematic viscosity of 1000 mm2/s (5000 SSU). The purchaser shall specify if this type of
lube system is to be supplied on units with frame ratings less than 150 kW (200 hp)
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6.14.2.1.4 The basic oil system, in accordance with 6.14.2.1.2, shall contain, as a minimum, the following components:
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6.14.2.3 Cooler
The following requirements apply to lube oil coolers.
a. Unless otherwise specified, when shell and tube coolers with surface area equal to or greater than 0.5 m2 (5 ft2) are supplied, a
removable-bundle design is required.
b. Removable-bundle coolers shall be in accordance with TEMA Class C or equivalent standard, and shall be constructed with a
removable channel cover.
c. Tubes shall not have an outside diameter of less than 16 mm (5/8 in.), and the tube shall have a wall thickness of not less than
1.2 mm (18 BWG).
d. Unless otherwise specified, cooler shells, channels and covers shall be steel; tube sheets shall be brass; and tubes shall be of a
copper/zinc/tin non-ferrous material such as UNS C44300.
e. U-bend tubes are not permitted.
f. Coolers shall be equipped with a high point vent and low point drain connections on their oil and water sides.
6.14.2.4 Filters
The following requirements apply to filters:
a. filters shall provide a minimum particle removal efficiency (PRE) for 10 μm particles of 90% (β10 >10) and a minimum PRE
of 99.5% for 15 μm particles (β15 >200), in both cases in accordance with ISO 16889 when tested to a minimum terminal
differential pressure of 3.5 bar (50 psig) (API 614, Chapter 3, 1.7.2);
b. cartridges shall have a minimum collapsing differential pressure of 5 bar (70 psig);
c. if size permits, each filter shall be equipped with a vent and clean- and dirty-side drain connections.
• 6.14.2.5
Heater
If specified, provisions to heat the oil for compressor start-up in cool ambient conditions shall be provided. Heating can be
supplied by:
a. a removable steam-heating element external to the reservoir,
b. a thermostatically controlled electric immersion heater, and
c. steam heating connections on the cooler.
Purchaser approval is required on the heating method.
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Electric immersion heaters should be interlocked to be de-energized when the oil level drops below the minimum operating level.
Note: Caution is required in using a steam heating connection on the cooler to avoid overheating the oil, or damage to the cooler.
• 6.14.2.6
Pressure Relief Valve
Each lube oil pump pressure relief valve shall be individually piped back to the crankcase reservoir. A relief valve serving the
main oil pump may have a cast iron or nodular iron body if it is located inside the crankcase; otherwise it shall be steel. If
specified, the relief valve for the crankcase-driven pump shall be mounted outside the crankcase. Continuously operating flowing
oil return lines shall enter the sump or an external reservoir in a way to avoid adverse effect on pump suction and electrostatic
discharge.
6.14.2.7 Oil Temperature Regulator
An oil temperature control system with a manual over-ride or bypass shall be provided. For water-cooled services, this system
shall be based on an arrangement by which a portion of the oil flow bypasses the cooler to maintain constant oil temperature to the
equipment. Control valves shall be of flanged steel construction. See Figure G-5 for a typical schematic drawing of a lube oil
system.
6.14.3 Cylinder and Packing Lubrication
6.14.3.1 General
• 6.14.3.1.1
The vendor shall supply either a single plunger-per-point or a divider-block mechanical lubricator system for
compressor cylinder and packing lubrication, as specified.
28
API STANDARD 618
• 6.14.3.1.2
Lubricators shall be driven by the crankshaft or driven independently, as specified. Lubricators shall be separate
from the frame lubrication pump(s) and complete with necessary tubing or piping (see 7.7.3). Ratchet lubricator drives shall not
be used.
6.14.3.1.3 Pumps shall be sized to permit a 100% increase and a 25% decrease in design flow. The pumps shall be designed to
allow adjustments to the pumping rate while the compressor is operating.
• 6.14.3.1.4
If specified, a lubricator reservoir heating device with thermostatic control shall be provided. The heat density of the
device shall be limited to 2.3 W/cm2 (15 W/in.2). The size of heating system and temperature control instrumentation shall be as
agreed by the purchaser and vendor. When an internal heater is used it shall be fully immersed even at minimum reservoir level
(see 6.14.3.2.1.2).
6.14.3.1.5 Unless otherwise specified, lubricators shall have provisions for pre-lubrication of the compressor prior to
compressor start up.
• 6.14.3.1.6
Each cylinder and packing lubrication system shall be provided with a lubricator system failure alarm. If specified,
additional alarm functions shall be provided (see 6.14.3.2.1.2 and 6.14.3.2.2).
6.14.3.1.7 At least one lubrication point shall be provided for each compressor cylinder bore and packing. A stainless steel
integral double-ball check valve shall be provided as close as possible to each lubrication point. Check valve, tubing and fittings
shall be rated for the maximum allowable working pressure of the lubricator. The check valve and tubing shall be arranged such
that the outlet of the check valve is always immersed in oil.
Note: The immersion in oil will aid in the valve sealing against gas pressure.
6.14.3.1.8 Lube oil injection passages to the cylinder bore shall be drilled through metal provided in the cylinder water jacket
casting or weldment. Lubrication pipes or tubes (similar to Figure G-2) running through the metal in the water jacket are
acceptable. Pipe or tubing shall be austenitic stainless steel as a minimum and may be used in the gas passages if the materials are
compatible with the gas composition (see 7.7.3). Lube oil injection passages shall be drilled and tapped for all cylinders including
non-lubricated services. Unused holes shall be plugged with threaded stainless steel solid plugs. Tubing connections shall be
match tagged for identification at the disassembly points for all compressor components in order to facilitate re-assembly.
• 6.14.3.1.9
If specified, the compressor cylinders, the compressor frame, or both, shall be lubricated by synthetic lubricants.
The lubricant specifications shall be mutually agreed between the purchaser and the vendor. Interior surfaces and non-metallic
components of the lubricating system coming into contact with synthetic lubricant shall be of compatible materials agreed by the
compressor manufacturer and the lubricant manufacturer. Interior surfaces coming in contact with synthetic lubricant shall be left
unpainted. In those cases where other interior surfaces (of distance pieces, or frames, for example) require painting, a synthetic
lubricant-resistant coating recommended by the lubricant manufacturer shall be used.
Note: The concerns with the use of synthetic lubricants are the contamination of conventional crankcase oil by synthetic cylinder lubricating oil,
and synthetic oil attack of paint coatings in the crankcase and distance pieces.
6.14.3.1.10 Lubricator reservoir capacity shall be adequate for a minimum of 30 hours of operation at normal flow rates.
6.14.3.2 Pump-to-point Lubrication
6.14.3.2.1 General
6.14.3.2.1.1 Lubricators shall have a sight flow indicator for each lubrication point.
6.14.3.2.1.2 Protection against loss of cylinder and packing lubrication shall consist of a low-pressure alarm connected to the
discharge of an extra plunger pump that circulates oil through an orifice and back to the lubricator reservoir. The plunger pump
shall have its suction tube shortened so that it will lose suction when the lubricator reservoir oil drops below 30% of full level.
When more than one reservoir compartment is used, each compartment shall be so protected.
• 6.14.3.2.2
Divider Block Lubrication
Divider block systems shall be provided with protection and indicating devices to protect the system from overpressure and to
allow operational monitoring of the functioning of the system.
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As a minimum, the following requirements shall be met:
a. each outlet of the primary divider block shall be equipped with a resettable spring-loaded indicator pin intended to signal that
the outlet is plugged;
b. the system shall be protected from overpressure with a relief device (rupture disc) located downstream of the pump(s);
c. a pressure gauge shall be provided indicating pump discharge pressure;
d. for protection against loss of flow, a cycle monitor shall be provided with a digital display showing total flow and shall be
equipped with an alarm indicating no flow;
e. the cycle monitor shall be driven by a proximity switch mounted on the primary divider block.
Additional, or alternative, protection and monitoring devices may be provided as agreed on by the purchaser and the vendor.
6.15 MATERIALS
6.15.1 General
6.15.1.1 Unless otherwise specified by the purchaser, the materials of construction shall be selected by the manufacturer based
on the operating and site environmental conditions specified.
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Annex H lists general material classes for compressors. When used with appropriate heat treatment and/or impact-testing
requirements, these material classes are considered acceptable for major component parts (see 7.7 for auxiliary piping material
requirements).
6.15.1.2 The materials of construction for all major components shall be clearly stated in the vendor's proposal. Materials shall
be identified by reference to applicable international standards, including the material grade (see Clause 2). Where international
standards are not available, internationally recognized national standards (such as AISI or ASTM) or other standards may be
used. When no such designation is available, the vendor's material specification, giving physical properties, chemical
composition, and test requirements shall be included in the proposal.
6.15.1.3 Copper and copper alloys shall not be used for parts of compressors or auxiliaries in contact with corrosive gas or with
gases capable of forming explosive copper compounds. Nickel-copper alloys (UNS N04400 Monel or its equivalent), babbitt
bearings, and precipitation-hardened stainless steels, are excluded from this requirement. Where mutually agreed between the
vendor and purchaser, copper-containing materials may be used for packing on lubricated compressors or other specific purposes.
Note: Certain corrosive fluids in contact with copper alloys have been known to form explosive compounds.
6.15.1.4 The vendor shall specify the optional tests and inspection procedures required to ensure that materials selected are
satisfactory for the service intended. Such tests and inspections shall be listed in the proposal.
• 6.15.1.5
Additional optional tests and inspections may be specified by the purchaser.
Note: At the purchaser’s request, additional optional tests and inspections can be specified, especially for materials used in critical components
or in critical services.
6.15.1.6 External parts that are subject to rotary or sliding motions (such as control linkage joints and adjustment mechanisms)
shall be of corrosion-resistant materials suitable for the site environment.
6.15.1.7 Minor parts such as nuts, springs, washers, gaskets, and keys shall have corrosion resistance at least equal to that of
specified parts in the same environment.
• 6.15.1.8
The presence of any corrosive agents (including trace quantities) in the motive and process fluids and in the site
environment, including constituents that can cause stress corrosion cracking, shall be specified by the purchaser.
Note 1: Typical agents of concern are hydrogen sulfide, amines, chlorides, cyanide, fluoride, naphthenic acid and polythionic acid.
Note 2: If chlorides are present in the process gas stream to any extent, extreme care must be taken with the selection of materials in contact with
the process gas. Caution should be given to components of aluminum and austenitic stainless steel.
6.15.1.9 If austenitic stainless steel parts exposed to conditions that may promote intergranular corrosion are to be fabricated,
hard faced, overlaid or repaired by welding, they shall be made of low-carbon or stabilized grades.
Note: Overlays or hard surfaces that contain more than 0.10% carbon can sensitize both low-carbon and stabilized grades of austenitic stainless
steel unless a buffer layer that is not sensitive to intergranular corrosion is applied.
30
API STANDARD 618
6.15.1.10 When mating parts such as studs and nuts of austenitic stainless steel or materials with similar galling tendencies are
used, they shall be lubricated with an antiseizure compound of the proper temperature specification and compatible with the
specified process fluid(s).
Note: With and without the use of antiseizure compounds, the required torque loading values to achieve the necessary preload will vary
considerably.
• 6.15.1.11
All materials exposed to H2S gas service as defined by NACE MR0175 shall be in accordance with the
requirements of that standard. Ferrous materials not covered by NACE MR0175 shall not have a yield strength exceeding
620 N/mm2 (90,000 psi) nor a hardness exceeding Rockwell C 22.
Components fabricated by welding shall be postweld heat treated, if required, so that both the welds and the heat-affected zones
meet the yield strength and hardness requirements.
Components expected to comply with NACE MR0175 shall include, as a minimum: all pressure-containing cylinder parts (such
as the cylinder, heads, clearance pockets, valve covers) and all fasteners directly associated with those parts; all components
within the cylinder (such as piston, piston rod, valves, unloaders and fasteners); components within the outboard distance piece
(such as packing box, packing, and fasteners).
Fasteners manufactured in accordance with NACE material requirements shall be clearly and permanently marked as such and
their correct locations shall be identified in the installation and maintenance manuals (see Annex Q).
On multiple service and multistage machines, NACE requirements shall apply to all fasteners and other interchangeable parts of
all cylinders to avoid possible inadvertent interchange of parts.
Hardness requirements for valve seats and piston rod surface can be in excess of NACE provisions (see 6.10.4.1). Similar
exceptions can be made for valve plates, springs, and unloader components, where greater hardness has been proven necessary.
Mutual agreement shall be reached between the vendor and the purchaser on requirements for alternative alloys or special heat
treatment.
Note: It is the responsibility of the purchaser to determine the expected amount of wet H2S, considering normal operation, start-up, shutdown,
idle standby, upsets, or unusual operating conditions such as catalyst regeneration.
In many applications, small amounts of wet H2S are sufficient to require materials resistant to sulfide stress corrosion cracking.
When there are trace quantities of wet H2S known to be present or if there is any uncertainty about the amount of wet H2S that
may be present, the purchaser should automatically note on the data sheets the requirement for materials resistant to sulfide stress
corrosion cracking.
6.15.1.12 The vendor shall select materials to avoid conditions that can result in electrolytic corrosion. Where such conditions
cannot be avoided, the purchaser and the vendor shall agree on the material selection and any other precautions necessary.
Note: When dissimilar materials with significantly different electrical potentials are placed in contact in the presence of an electrolytic solution,
galvanic couples can be created that can result in serious corrosion of the less noble material. The NACE Corrosion Engineer’s Reference Book
is one resource for selection of suitable materials in these situations.
6.15.1.13 Low-carbon steels can be notch sensitive and susceptible to brittle fracture at ambient or lower temperatures.
Therefore, only fully killed, normalized steels made to fine-grain practice are acceptable. The use of steel made to a coarse
austenitic grain size practice (such as ASTM A 515) shall be avoided.
6.15.1.14 O-ring materials shall be compatible with all specified services. Special consideration shall be given to the selection
of O-rings for high-pressure services to ensure that they will not be damaged upon rapid depressurization (explosive
decompression).
Note: Susceptibility to explosive decompression depends on the gas to which the O-ring is exposed, the compounding of the elastomer,
temperature of exposure, the rate of decompression, and the number of cycles.
6.15.1.15 The minimum quality bolting material for pressure joints shall be carbon steel such as ASTM A 307, Grade B for
cast iron components, and high temperature alloy steel such as ASTM A 193, Grade B7 for steel or ductile iron components.
Carbon steel nuts such as ASTM A 194, Grade 2H shall be used. For minimum allowable temperatures equal to or lower than –
30°C (–20°F), low-temperature bolting material such as ASTM A 320 shall be used.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
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6.15.1.16 The corrosion allowance for separate carbon-steel knockout pots shall be a minimum of 3 mm (1/8 in.). The
purchaser and the vendor shall agree upon the corrosion allowance for heat exchangers and alloy parts required for special
services.
6.15.2 Pressure-containing Parts
6.15.2.1 Unless otherwise specified, materials for pressure-containing cylinder parts shall be used in conjunction with the
maximum allowable working pressure (MAWP) in Table 3. All material selections shall be subject to review by the purchaser.
Note: Higher design pressures may be permitted based on detailed engineering analysis.
Table 3—Maximum Gauge Pressures for Cylinder Materials
Material
Gray cast iron
Nodular iron
Cast steel
Forged steel
Fabricated steel
Maximum Allowable Working Pressure
bar
70
100
180
psig
1000
1500
2500
No limitation
85
1250
6.15.2.2 Steel compressor cylinders shall be equipped with steel heads.
6.15.2.3 The use of fabricated cylinders shall be stated in the proposal, and requires the purchaser’s written approval.
6.15.3 Castings
6.15.3.1 General
6.15.3.1.1 Castings shall be sound and free of shrink holes, blowholes, cracks, scale, blisters, and similar injurious defects.
Surfaces of castings shall be cleaned by sandblasting, shot-blasting, chemical cleaning, or other standard methods. Mold-parting
fins and the remains of gates and risers shall be chipped, filed, or ground flush.
Castings shall not be impregnated or surface sealed at the foundry prior to machining.
6.15.3.1.2 The use of chaplets in pressure castings shall be held to a minimum. Where chaplets are necessary, they shall be
clean and corrosion free (plating is permitted) and of a composition compatible with the casting.
6.15.3.1.3 Fully enclosed cored voids, which become fully enclosed by methods such as plugging, welding, or assembly, are
prohibited.
6.15.3.1.4 Unless otherwise specified, pressure-retaining castings of gray iron shall be produced in accordance with ASTM
A 278, and pressure-retaining castings of steel shall be produced in accordance with ASTM A 216.
6.15.3.2 Nodular Iron Castings
6.15.3.2.1 Nodular iron castings shall be produced in accordance with an internationally recognized standard such as ASTM
A 395. The production of the castings shall conform to the conditions specified in 6.15.3.2.2 through 6.15.3.2.5.
6.15.3.2.2 A minimum of one set (three samples) of Charpy V-notch impact specimens at one-third the thickness of the test
block shall be made from the material adjacent to the tensile specimen on each keel or Y-block. All three specimens shall have an
impact value not less than 12 J (9 ft-lb) and the mean of the three specimens shall not be less than 14 J (10 ft-lb) at room
temperature.
6.15.3.2.3 The keel or Y-block cast at the end of the pour shall have a thickness not less than the thickness of critical sections
of the main casting. This test block shall be tested for tensile strength and hardness and shall be microscopically examined.
Classification of graphite nodules under microscopic examination shall be in accordance with ASTM A 247.
6.15.3.2.4 An “as-cast” sample from each ladle shall be chemically analyzed.
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API STANDARD 618
6.15.3.2.5 To verify the uniformity of the casting, Brinell hardness readings shall be made on the actual castings at section
changes, flanges, and other accessible locations such as the cylinder bore and valve ports. Sufficient surface material shall be
removed before hardness readings are made to eliminate any skin effect. Readings shall also be made at the extremities of
castings at locations that represent the sections poured first and last. These readings shall be made in addition to Brinell readings
on the keel and Y-blocks.
6.15.4 Forgings
Pressure-containing forgings shall be in accordance with ASTM A 668.
6.15.5 Fabricated Cylinders and Cylinder Heads
6.15.5.1 When fabricated cylinders are allowed, they shall be designed based on an infinite fatigue life. The vendor shall
conduct an engineering analysis that addresses the applicable loads, materials, weldments, and the geometry of the cylinder. The
analysis shall ensure that the alternating stresses are limited to values that preclude the propagation of an existing internal defect.
6.15.5.2 Gas pressure-containing parts of cylinders and cylinder heads made of wrought materials or combinations of wrought
and cast materials shall conform to the conditions specified in 6.15.5.3 through 6.15.5.13.
6.15.5.3 Plate subjected to alternating pressure loads used in cylinders and cylinder heads shall be subjected to the procedures
in 6.15.5.4 through 6.15.5.6 after being cut to shape and before weld joint preparation.
6.15.5.4 If the plate is loaded in tension in the through-thickness direction, the surface shall be 100% ultrasonically inspected
in the area one plate-thickness on each side of the load-imposing member (see Figure 1).
Figure 1—Plate Loaded in Tension in the Through-thickness Direction and its Area Requiring Ultrasonic Inspection
6.15.5.5 If the plate is loaded in bending, the surface shall be 100% ultrasonically inspected in the area one plate-thickness on
each side of the load-imposing member (see Figure 2).
6.15.5.6 If the plate is axially loaded, ultrasonic inspection is not required (see Figure 3).
Note: These procedures are intended to discover laminations or inclusions that can affect the load-carrying ability of the components.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
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Figure 2—Plate Loaded in Bending and its Area Requiring Ultrasonic Inspection
Figure 3—Axially Loaded Plate
6.15.5.7 After preparation for welding, plate edges shall be inspected by magnetic particle or liquid penetrant examination as
required by the specified pressure vessel code or internationally recognized standard such as ASME Section VIII, Division 1,
UG-93 (d)(3).
6.15.5.8 Accessible surfaces of welds shall be inspected by magnetic particle or liquid penetrant examination after chipping or
back-gouging and again after post-weld heat treatment.
6.15.5.9 Unless approved by the purchaser prior to the start of fabrication, pressure-containing welds, including welds to
horizontal- and vertical-joint flanges, shall be full-penetration (complete-joint) welds.
6.15.5.10 All fabricated cylinders and cylinder heads shall be post-weld heat treated, regardless of thickness (see 6.15.7.7).
6.15.5.11 All butt welds on the inner barrel of welded cylinders shall be 100% examined radiographically. Other welds to the
inner barrel shall be inspected radiographically where possible. If radiography is not possible, other methods such as ultrasonic
examination shall be used.
• 6.15.5.12
If specified, in addition to the requirements of 6.15.7.1, specific welds shall be subjected to 100% radiography,
magnetic particle inspection, or liquid penetrant inspection.
• 6.15.5.13
If specified, proposed cylinder, cylinder-head, and connection designs shall be made available for review and
approval by the purchaser before fabrication. The drawings shall show weld designs, size, materials, and pre-weld and post-weld
heat treatments.
6.15.6 Repairs to Castings and Forgings
6.15.6.1 Major repairs to pressure-containing parts, all repairs to moving parts subject to load reversals, and all repairs to
crankshafts shall not be undertaken without the purchaser’s written authorization. This can include, but not be limited to, cylinder
parts, piston and rod assembly components, and crosshead assembly components.
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API STANDARD 618
6.15.6.2 A major repair, for the purpose of purchaser notification, is any defect that equals or exceeds any of the following
criteria:
a. any repair of a pressure-containing part in which the depth of the cavity prepared for repair welding exceeds 50% of the
component wall thickness, and/or is longer than 150 mm (6 in.) in any direction;
b. any situation where the total area of all repairs to the part under repair exceeds 10% of the surface area of the part;
c. any repairs to pressure containing parts carried out after hydrostatic testing.
a.
b.
c.
d.
e.
sketches showing the defective area;
proposed method of repair;
materials to be used;
welding procedure;
proposed extent of testing or re-testing to prove the effectiveness of the repair.
All such repairs shall be properly documented for the purchaser’s permanent record.
6.15.6.4 For non-pressure-containing components, the vendor shall make repairs in accordance with his internal quality
procedures. These procedures shall be available for review by the purchaser at the manufacturer’s plant.
When repairs of non-pressure-containing components are done, they must be documented by the vendor. No repair is to be made
without written approval of the vendor’s engineering, quality-control, and manufacturing departments.
• 6.15.6.5
If specified, the purchaser shall be given notice of repairs to other major components, such as distance pieces, and
crankcase.
6.15.6.6 Pressure-containing castings shall not be repaired by peening, burning-in, or impregnating. Pressure-containing
castings and forgings shall not be repaired by welding, plating, or plugging except as specified in 6.15.6.7 through 6.15.6.8.
6.15.6.7 Weldable grades of steel castings and forgings may be repaired by welding using a qualified welding procedure (see
6.13.7.3). After major weld repairs but before hydrostatic testing, the complete casting or forging shall be given a post-weld heat
treatment to ensure stress relief and continuity of mechanical properties of both weld and parent metals.
6.15.6.8 Gray cast iron or nodular iron may be repaired by plugging within the limits specified in the applicable material
standard such as ASTM A 278 or A 395; but shall not be repaired by welding.
Unless mutually agreed by the purchaser and the vendor, plugs shall not be used in the gas-pressure-containing wall sections of
cylinders: in particular in the bore under the liner.
When plugs are allowed, the holes drilled for plugs shall be carefully examined, using liquid penetrant, to ensure that all defective
material has been removed.
Note: Annex D describes some repair techniques that can be considered for application to gray or nodular iron castings for compressor
cylinders. These techniques should only be applied after a thorough mutual evaluation of the circumstances by the purchaser and the vendor.
6.15.7 Welding
6.15.7.1 Welding of piping, pressure-containing parts, rotating parts and other highly stressed parts, weld repairs, and any
dissimilar-metal welds shall be performed and inspected by procedures and operators qualified in accordance with the specified
pressure design code or internationally recognized standards such as ASME Section VIII, Division l, and ASME Section IX.
6.15.7.2 Unless otherwise specified, other welding, such as welding on baseplates, non-pressure ducting, lagging, and control
panels, shall be performed by welders qualified in accordance with an appropriate recognized standard such as AWS D 1.1.
6.15.7.3 The vendor shall be responsible for the review of all repairs and repair welds. The vendor shall also be responsible to
ensure that all the repairs and repair welds are properly heat treated and nondestructively examined for soundness, and to ensure
compliance with the applicable qualified procedures.
Repairs shall be nondestructively tested by the same method used to detect the original flaw. However, the minimum level of
inspection after the repair, shall be by the magnetic particle method in accordance with 8.2.2.4 for magnetic material and by the
liquid penetrant method in accordance with 8.2.2.5 for nonmagnetic material.
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6.15.6.3 Before performing major repairs to pressure containing parts, the vendor shall submit the following for the
purchaser’s written approval:
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
35
Unless otherwise specified, weld procedures for major repairs shall be subject to review by the purchaser prior to any repair.
6.15.7.4 Connections welded to pressure-containing parts shall be installed as specified in 6.15.7.5 through 6.15.7.9.
If specified, in addition to the requirements of 6.15.7.1, specific welds shall be subjected to 100% radiography or
• 6.15.7.5
magnetic particle inspection or liquid penetrant inspection of welds.
If specified, proposed connection designs shall be submitted to the purchaser for acceptance before the start of
• 6.15.7.6
fabrication. The drawings shall show weld designs, size, materials, and pre- and postweld heat treatments.
6.15.7.7 All welds shall be heat treated in accordance with the specified pressure vessel code or an internationally recognized
standard such as the ASME Section VIII, Division 1, Sections UW-10 and UW-40. For steels in H2S service, heat treatment shall
also be in accordance with NACE MR0175 (see 6.15.1.11).
6.15.7.8 If postweld heat treatment is required it shall be carried out after all welds, including piping welds, have been
completed.
6.15.7.9 Auxiliary piping welded to alloy steel casings and cylinders shall be of a material with the same nominal properties as
the casing or cylinder material or shall be of low carbon austenitic stainless steel. Other materials compatible with the casing or
cylinder material and intended service may be used with the purchaser's approval.
6.15.7.10 Flux-core welding may be used for equipment in hydrogen service, upon written agreement of the purchaser after
submission of weld procedures.
6.15.8 Low-temperature Service
• 6.15.8.1
The minimum design metal temperature and concurrent pressure used to establish impact test and other material
requirements shall be as specified.
Note: Minimum temperature can be caused by operating and/or environmental conditions including auto-refrigeration, and low ambient
temperatures during shipping, installation, operation or shutdown.
6.15.8.2 To avoid brittle failures, materials and construction for low temperature service shall be suitable for the minimum
design metal temperature in accordance with the codes and other requirements specified. The purchaser and the vendor shall
agree on any special precautions necessary with regard to conditions that can occur during operation, maintenance, transportation,
erection, commissioning and testing.
6.15.8.3 All carbon and low alloy steel pressure-containing components, including nozzles, flanges, and weldments, shall be
impact tested in accordance with the requirements of ASME Section VIII, Division 1, Sections UCS-65 through 68, or the
specified pressure design code. High-alloy steels shall be tested in accordance with ASME Section VIII, Division l, Section
UHA-51, or the specified pressure design code. For materials and thickness’ not covered by ASME Section VIII, Division l or the
specified pressure design code, testing requirements shall be as specified by the purchaser.
Note: Impact testing of a material may be omitted depending on the minimum design metal temperature, thermal, mechanical and cyclic loading
and the governing thickness. Refer to requirements of ASME Section VIII, Division l, Section UG-20F, for example.
6.15.8.4 The governing thickness used to determine impact testing requirements shall be the greater of the following.
a. The nominal thickness of the largest butt-welded joint.
b. The largest nominal section for pressure containment, excluding
1. structural support sections such as feet or lugs,
2. sections with increased thickness required for rigidity to mitigate shaft deflection,
3. structural sections required for attachment or inclusion of mechanical features such as jackets or seal chambers;
c. One fourth of the nominal flange thickness (recognizing that the predominant flange stress is not a membrane stress).
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Note: Good design practice should be followed in the selection of fabrication methods, welding procedures, and materials for vendor furnished
steel pressure-retaining parts that can be subject to temperatures below the ductile-to-brittle transition temperature. The published designallowable stresses for many materials in internationally recognized standards such as the ASME Code and ANSI standards are based on
minimum tensile properties. Some standards do not differentiate between rimmed, semi-killed, fully-killed hot-rolled, and normalized material,
nor do they take into account whether materials were produced under fine- or course-grain practices. The vendor should exercise caution in the
selection of materials intended for services between –30°C (–20°F) and 40°C (100°F).
36
API STANDARD 618
The results of the impact testing shall meet the minimum impact energy requirements of ASME Section VIII, Division l, Section
UG-84, or the specified pressure design code.
Note: Selecting materials that do not require impact testing is usually preferable to using materials that necessitate impact testing. Some codes
(such as ASME) do not require impact tests under certain specific conditions.
6.15.8.5 The purchaser and vendor shall mutually agree upon testing requirements for highly stressed machine parts, such as
shafts.
6.16 NAMEPLATES AND ROTATION ARROWS
6.16.1 A nameplate shall be securely attached at a visible location on the compressor frame, on each compressor cylinder, and
on any major piece of auxiliary equipment.
6.16.2 Rotation arrows shall be cast-in or attached to each major item of rotating equipment at a readily visible location.
6.16.3 Nameplates and rotation arrows (if attached) shall be of austenitic stainless steel or nickel-copper (UNS N04400 alloy).
Attachment pins shall be of the same material. Welding is not permitted.
6.16.4 The following data shall be clearly stamped or engraved on the frame nameplate:
a.
b.
c.
d.
e.
f.
vendor’s name;
serial number;
frame size and model;
rated speed;
stroke;
purchaser item number or other reference.
6.16.5 Nameplates on compressor cylinders shall include the following data:
a.
b.
c.
d.
e.
f.
g.
h.
vendor’s name;
serial number;
bore, stroke, model number;
maximum allowable working pressure;
hydrostatic test pressure;
maximum allowable working temperature;
cold piston end-clearance setting for each end;
minimum allowable temperature (required if the material is rated for a minimum allowable temperature below –20°C).
6.16.6 Induction motors used for driving reciprocating compressors shall be provided with an auxiliary nameplate stating the
expected full-load current, and the expected current pulsation level based on the flywheel selection and resulting final inertia of
the rotating system.
Note: The standard motor nameplate current is normally based on steady-state loads and is not always valid for the variable torque loads
imposed by reciprocating compressor (see note in 7.1.2.6).
• 6.16.7
The purchaser shall specify whether USC or SI units are to be shown on nameplates.
7 Accessories
7.1 DRIVERS
7.1.1 General
Unless otherwise specified, the compressor vendor shall furnish the driver and power transmission equipment. The type
• 7.1.1.1
of driver shall be as specified by the purchaser.
7.1.1.2 The driver shall be sized to meet the maximum specified operating conditions, including external power transmission
losses and shall be in accordance with applicable specifications as stated in the inquiry and order. The driver shall operate under
the utility and site conditions specified in the inquiry.
7.1.1.3 The driver shall be capable of driving the compressor with all stages at full flow and discharging at the relevant relief
valve set pressure.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
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7.1.1.4 The driver shall be sized to accept any specified process variations such as changes in the pressure, temperature or
properties of the fluids handled, and plant start-up conditions.
• 7.1.1.5
The purchaser shall specify anticipated process variations that can affect the sizing of the driver (such as changes in the
pressure, temperature or properties of the fluid handled, as well as special plant start-up conditions).
• 7.1.1.6
The purchaser shall specify the starting conditions for the driven equipment. The starting procedure shall be agreed by
the purchaser and the vendor. The driver’s starting-torque capabilities shall exceed the starting-torque requirements of the driven
equipment from zero to operating speed.
7.1.1.7 The inertial characteristics of the rotating parts of the compressor and of the drive train shall be such that rotational
oscillations will be minimized. Undesirable oscillations include those that cause damage, undue wear of parts or interference with
the governor or governing system of the driver and those that result in harmful torsional and/or electrical system disturbances. For
initial design purposes, peak-to-peak speed oscillation of the rotating system shall be limited to 1.5% of rated speed at full load
and partial cylinder loads if step unloading is specified.
The compressor vendor shall inform the driver manufacturer of the nature of the application including the torque variation
characteristics, and shall obtain confirmation from the driver manufacturer that the driver is suitable for this service.
7.1.1.8 For purposes of sizing flywheels and couplings for gear drives, the peak-to-peak torque variation at the gear shall not
exceed 25% of the torque corresponding to the maximum compressor load and in no case shall there be any torque reversal in the
gear mesh.
7.1.1.9 For belt-driven compressors the peak-to-peak speed variation shall not exceed 3% of rated compressor speed at any
operating condition (see 7.4).
7.1.1.10 The supporting feet of drivers with a mass greater than 250 kg (500 lb) shall be provided with vertical jackscrews.
7.1.2 Motor Drivers
• 7.1.2.1
The type of motor supplied and its characteristics and accessories, including but not limited to the following, shall be as
specified by the purchaser:
a. type of motor (synchronous or induction);
b. bearing arrangement;
c. electrical characteristics;
d. starting conditions (including the expected voltage drop on starting);
e. the type of enclosure;
f. the sound pressure level;
g. the area classification, based on IEC 60079, API 500, or equivalent international standard;
h. the insulation class and maximum temperature rise;
i. the required service factor;
j. the ambient temperature and elevation above sea level;
k. electrical transmission losses;
l. temperature detectors, vibration sensors, and heaters specified;
m. auxiliaries (such as motor generator sets, ventilation blowers, and instrumentation);
n. vibration acceptance criteria;
o. use in variable frequency drive applications;
p. any power factor requirement;
q. applicability of the various parts of IEC 60034, API 541 or 546, or IEEE 841.
If belt drives are required, see 7.4.3.
7.1.2.2 For motor-driven units, the motor rating, inclusive of service factor, shall be not less than 105% of the power required
(including power transmission losses) for the relieving operation specified in 7.1.1.3. In addition, the motor rating, exclusive of
service factor, shall be not less than 110% of the greatest power required (including power transmission losses) for any of the
specified operating conditions.
Note: The 110% is a design criterion. After testing, this margin might not be available due to performance tolerances of the driven equipment.
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38
•
API STANDARD 618
7.1.2.3 If specified, single bearing motors shall be provided with a temporary inboard support device to facilitate erection and
alignment.
• 7.1.2.4
The motor’s starting torque shall meet the requirements of the driven equipment, at a reduced voltage of 80% of the
normal voltage, or other specified value, and the motor shall accelerate to full speed within 15 seconds or other period of time
agreed by the purchaser and the vendor. The motor starting-torque shall be sufficient to start the compressor without the need to
depressurize any stage from its normal suction pressure as long as all cylinder ends are unloaded or all stages are 100% bypassed.
Special agreement may be necessary in the following circumstances: low ratios of piston-to-rod diameters; high suction pressure;
high settling-out gas pressure specified by the purchaser; high-pressure unloaded starts; or alternate gas unloaded starts.
7.1.2.5 Unless otherwise specified, the design of the motor shall conform to either IEC 60034-1, IEC 60079, and IEC 60529, or
to NFPA 70 and NEMA MG 1.
7.1.2.6 The combined inertia of rotating parts of synchronous motor-compressor installations shall be sufficient to limit motor
current variations to a value not exceeding 66% of the full load current (see IEC 60034 or NEMA MG1) for all specified loading
conditions, including unloaded operation with cylinders pressurized to their normal suction pressures. For induction motorcompressor installations, motor current variations shall not exceed 40% of the full load current using the method described in IEC
60034 or NEMA MG1. The electrical system data necessary for proper design shall be provided by the purchaser.
Note: The power supply for some installations can require tighter control of current variations to protect other equipment in the electrical
system. Standard motor performance data are based on steady-state load conditions and may not reflect actual performance under the variabletorque conditions encountered when driving reciprocating compressors. With induction-motor drivers, the effects of variable torque and
resultant current pulsations are more pronounced and require closer evaluation (see 6.7.4 and 7.1.1.7).
For this reason, high-efficiency induction motors with their lower slip factors can experience higher current pulsations and
consequently draw higher average current and higher power than standard efficiency motors when driving reciprocating
compressors.
High-efficiency motors will create higher axial forces when they are not mounted on magnetic center.
High-efficiency induction motors are more suited to driving steady-state loads such as fans and blowers.
7.1.2.7 When the motor is supplied by the purchaser, the compressor vendor shall furnish the purchaser with the following:
a. the required motor rotor inertia to satisfy the flywheel requirements of the compressor for all specified operating conditions;
b. starting-torque requirements;
c. mounting or coupling details, or both.
7.1.2.8 The rotor of a cantilevered (overhung) or single-bearing motor driver shall be mounted on a shaft extension with a
keyed interference fit. The shaft extension shall be rigidly coupled to the crankshaft, with forged flanges integral with the motor
shaft and crankshaft. Split or clamped hubs shall not be used. The interference fit shall carry the maximum transmitted torque by
itself; the key shall not be relied on to carry any of the torque. Side clearance for the key shall be 0.025 mm (0.001 in.) at
maximum. Top clearance for the key shall be adequate to prevent overstressing of the keyway. Keyless interference fits are
acceptable only if accepted by the purchaser. Keys and keyways shall be machined with smooth, generous radii to minimize the
effects of stress concentration. An outboard bearing shall be provided by the vendor to support the end of the shaft extension on
all engine-type induction and synchronous motors.
Note: Motors, usually synchronous, where the shaft extension is supplied separately from the motor rotating electrical parts are typically
referred to as being of engine-type construction.
7.1.2.9 Where a synchronous motor is to be connected to an electrical bus system that feeds existing synchronous motors, the
purchaser shall perform an electrical system analysis and supply the compressor vendor (and the motor vendor if the motor is
separately purchased) with all data necessary to permit proper design.
7.1.2.10 For synchronous-motor-driven compressors, the torsional stiffness and the inertia of all rotating parts shall provide at
least a 20% difference between any inherent exciting frequency of the compressor and the torsional frequency of the motor rotor
oscillation with respect to the rotating magnetic field.
7.1.2.11 Unless otherwise specified, the necessary motor starting apparatus shall be supplied by the purchaser.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
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7.1.2.12 Unless specified, cantilevered (overhung) motors shall not be supplied. If specified, cantilevered motor shafts shall
have sufficient rigidity to prevent the main rotor and rotating exciter, if fitted, from contacting their stators as a result of either
shaft deflection and unbalanced magnetic forces or dynamic mechanical unbalanced forces.
7.1.2.13 For cantilevered (overhung) and single bearing motors, the motor manufacturer’s drawing shall show the allowable
tolerance for setting the air gap. All sections of the motor (and rotary exciter, if applicable) stator shall be doweled after internal
alignment is completed to ensure maintenance of the proper air gap. The exciter housing (if applicable) shall be mounted with
sufficient lateral and axial rigidity to prevent excessive motion of the stator relative to the rotor.
7.1.2.14 Motors without thrust bearings shall be provided with a permanent and evident indication of the position of the rotor
relative to the axial magnetic center.
•
7.1.2.15 The bearings of motors rigidly coupled to a compressor shall be of the same generic type (hydrodynamic or rolling
element) as the main bearings of the driven compressor. The use of rolling element bearings in other cases shall be subject to the
purchaser’s approval. The design of direct coupled motors shall be such, that the bearings can be inspected, removed and replaced
in-situ.
Bearings shall be electrically insulated to prevent the circulation of stray electrical currents. Bearing supports shall have
provisions for adjustment shims. Hydrodynamic bearings shall be self-lubricated (e.g., oil-ring and sump) or, if specified, shall
receive lubricating oil from the compressor frame lubrication system.
Bearing housings shall be provided with shaft seals to prevent the ingress of dirt and moisture into the bearings or the leak of oil
into the motor windings. If specified, for pedestal mounted bearings, an NPS 1/4 drilled, tapped, and plugged hole shall be
provided for connection of a dry air purge.
7.1.2.16 The motors for auxiliary equipment shall be suitable for the specified area classification in accordance with either IEC
60079 and IEC 60529, or NFPA 70, Article 500. Motor rating (exclusive of service factor) shall be at least 110% of the maximum
power required for any operating condition.
7.1.3 Turbine Drivers
• 7.1.3.1
Steam turbine drivers shall conform to ISO 10436 or ISO 10437 or API 611 or API 612. The turbine power rating, shall
be not less than 110% of the power required (including power transmission losses) for the relieving operation specified in 7.1.1.3
with the specified normal steam conditions. In addition, the turbine continuous power rating shall be no less than 120% of the
greatest power required, (including any power transmission losses) when operating at any of the specified operating conditions,
with the specified normal steam conditions.
Note 1: The 120% factor includes an allowance for the cyclic torque load of reciprocating compressors.
Note 2: The 120% is a design criterion. After testing, this margin might not be available due to performance tolerances of the driven equipment.
• 7.1.3.2
If specified, a separate special-purpose lube oil system in accordance with ISO 10438-2 or API 614, Chapter 2, shall be
furnished for a turbine drive train.
7.2 COUPLINGS AND GUARDS
7.2.1 Couplings
7.2.1.1 When a coupling is required between the driver and the driven equipment, it shall be supplied by the manufacturer of
the driven equipment.
7.2.1.2 Unless otherwise specified, a flexible coupling shall be supplied. The coupling shall be of the all-steel, non-lubricated,
flexible membrane, torsionally-rigid, spacer-type. For low speed applications, couplings may be of the elastomeric type where
necessary to avoid torsional resonance problems. The coupling type, manufacturer, model, and mounting arrangement shall be
mutually agreed upon by the purchaser and the vendors of the driver and driven equipment.
Note: For information on torsional damping couplings and resilient couplings see ISO 10441 or API 671, Appendix B.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`-
• 7.2.1.3
If specified, the coupling or couplings shall be special purpose couplings conforming to ISO 10441 or API 671.
Coupling mountings shall conform to ISO 10441 or API 671.
Note: The purchaser should provide a list of preferred coupling manufacturers.
40
API STANDARD 618
7.2.1.4 For compressors rated at 1500 kW (2000 hp) or more and driven by a double-reduction gear, the low-speed coupling
can be a quill shaft. In such cases, the quill shaft shall be directly coupled to the compressor flywheel, shall pass through the
hollow low-speed gear shaft, and shall couple with the low-speed shaft on the side opposite the compressor.
Stresses in the quill shaft shall be given consideration.
Note: A typical value for the mean torsional stress is approximately 15% of the yield strength of the material. The alternating stress is typically
held to a value no greater than one third of the mean torsional stress.
7.2.1.5 Information on shafts, keyway dimensions (if any) and shaft end movements due to end play and thermal effects shall
be furnished to the vendor supplying the coupling.
Note: This information is normally furnished by the vendor of the driven equipment or the driver vendor.
7.2.1.6 The coupling-to-shaft juncture shall be designed and manufactured to be capable of transmitting power at least equal to
the power rating of the coupling.
• 7.2.1.7
If specified, couplings for auxiliary drives shall be in accordance with ISO 14691 or API 677.
7.2.1.8 Unless otherwise specified, couplings shall be mounted in accordance with the requirements of 7.2.1.9 through
7.2.1.11.
7.2.1.9 Flexible couplings shall be keyed to the shaft. Keys and keyways and their tolerances shall conform to ISO R773,
normal fit or equivalent such as AGMA 9002, Commercial Class.
7.2.1.10 Flexible couplings with cylindrical bores shall be mounted with an interference fit. Cylindrical shafts shall comply
with AGMA 9002 and the coupling hubs shall be bored to the following tolerances per ISO 286-2:
a. for shafts of 50 mm (2 in.) diameter and smaller—Grade N7;
b. for shafts larger than 50 mm (2 in.) diameter—Grade N8.
7.2.1.11 Coupling hubs shall be furnished with tapped puller holes at least 10 mm (0.375 in.) diameter to facilitate removal.
7.2.2 Guards
• 7.2.2.1
Guards shall be provided by the vendor for each coupling, auxiliary drive coupling and all moving parts which might be
hazardous to personnel. Guards shall comply with specified applicable safety codes.
7.2.2.2 Coupling and flywheel guards shall sufficiently enclose the coupling, flywheel, and the shafts to prevent any personnel
from accessing the space between the guard and such moving parts during operation of equipment train.
7.2.2.3 Guards shall be constructed with sufficient rigidity to withstand a 900 N (200 lbf) static point load in any direction
without the guard contacting moving parts.
7.2.2.5 For outdoor installations, guards over belt and chain drives shall be weatherproofed and properly ventilated to prevent
excessive heat build up. A weatherproof access door (or doors) shall be provided as necessary to allow inspection and servicing of
belts and chains.
7.3 REDUCTION GEARS
• 7.3.1
Gear units shall be either special purpose units conforming to ISO 13691 or API 613, or general purpose units
conforming to API 677, as specified.
7.3.2 Gears lubricated by an integral pump shall be provided with an electrically driven standby pump arranged for automatic
start. The system shall be arranged to prevent starting unless the oil pressure has reached the minimum permissible level.
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7.2.2.4 Unless otherwise specified, guards may be constructed of either metallic or nonmetallic materials. Guards shall be
easily removable, weatherproof, and of non-sparking construction. Guards shall have no openings, except that openings with
removable covers shall be provided in flywheel guards for barring-over the machine and for access to indicator timing marks,
wheel center (if available) and to any other parts which can require attention. Metallic guards shall preferably be fabricated from
continuously welded solid sheet or plate. Guards fabricated from expanded metal or perforated sheets are acceptable, providing
the size of the openings does not exceed 10 mm (0.375 in.) diameter. Guards of woven wire are not acceptable.
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
41
7.4 BELT DRIVES
7.4.1 Belt drives shall only be used for equipment of 150 kW (200 hp) or less and require purchaser approval. Belt drives up to
225 kW (300 hp) may be proposed for purchaser’s acceptance. Unless otherwise specified, timing type belts and sheaves shall be
provided. All belts shall be of the static-conducting type and shall be oil resistant. The drive service factor shall not be less than
1.75 based on the driver nameplate power rating.
If other than timing type belts are used, the details of belt tension, center distance, belt wrap and crankshaft web deflection and
testing shall be mutually agreed by the vendor and purchaser.
7.4.2 The vendor shall provide a positive belt-tensioning device on all belt drives. All bearing lubrication points shall be
accessible.
7.4.3 When a belt drive is to be used, the vendor who has unit responsibility shall inform other manufacturer(s) of the
connected equipment. The other manufacturer(s) shall be provided with the radial load resulting from the belt drive and, the
torque variation characteristics. The drive manufacturer shall take into account the radial load and torque variation conditions and
shall provide bearings with a life at least equivalent to that specified in 6.11.2.2.
7.4.4 Belt drives shall meet the following requirements:
a. the distance between the centers of the sheaves shall be at least 1.5 times the diameter of the larger sheave;
b. the belt wrap (contact) angle on the smaller sheave shall be at least 140º;
c. the shaft length on which the sheave hub is fitted shall be greater than or equal to the width of the sheave hub;
d. the length of a shaft key, if used, to mount a sheave shall be equal to the length of the sheave bore;
e. unless otherwise specified, each sheave shall be mounted on a tapered adapter bushing;
f. to reduce the overhang moment on shafts due to belt tension the sheave overhang distance from the adjacent bearing shall be
minimized;
g. sheaves, and mounting hardware, shall meet the balance requirements of ISO 1940-1 (ANSI S2.19, Grade 6.3).
7.5 MOUNTING PLATES
7.5.1 General
• 7.5.1.1
The equipment shall be furnished with a baseplate, a skid, soleplates, or rails as specified.
Note: See Appendix L for typical mounting plate and soleplate arrangements.
7.5.1.2 Machinery mounting plates shall be designed to avoid relative displacement of the frame and mounting plate.
7.5.1.3 Mounting plates shall conform to the following:
a. mounting plates shall not be drilled for equipment to be mounted by others;
b. mounting plates intended for installation on concrete shall be supplied with leveling screws;
c. outside corners of mounting plates which are in contact with the grout shall have 50 mm (2 in.) minimum radiused outside
corners (in the plan view);
d. bottom corners of mounting plates that are in contact with grout shall be radiused or chamfered;
e. all machinery mounting surfaces that are not to be grouted shall be treated with a rust preventive immediately after machining;
f. mounting plates shall extend at least 25 mm (1 in.) beyond the outer three sides of equipment feet.
7.5.2 Machined Surfaces
7.5.2.1 The upper and lower surfaces of driver bearing pedestals shall be machined parallel. The surface finish shall be 3.2 μm
(125 µin.) Ra (arithmetic average roughness) or better.
7.5.2.2 When equipment is mounted directly on machined metal surfaces integral with mounting plates, such surfaces shall
a. be machined after the baseplate is fabricated.
b. be flat and parallel to all other mounting surfaces within 0.15 mm/m (0.002 in./ft), and
c. have a surface finish of 3.2 μm (125 µin.) Ra (arithmetic average roughness) or better.
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42
API STANDARD 618
7.5.3 Leveling, Alignment, and Lifting
7.5.3.1 Mounting plates shall have jackscrews conforming to the following.
a. The compressor parts (such as a crankcase or a crosshead frame) shall be equipped with vertical jackscrews.
b. The feet of the drive equipment shall be equipped with vertical jackscrews.
c. When the drive equipment mass exceeds 450 kg (1000 lb), the drive train mounting plates shall be furnished with horizontal
jackscrews (axial and lateral) the same size as, or larger than, the vertical jackscrews. The lugs holding the jackscrews shall be
attached to the mounting plates so that they do not interfere with the installation or removal of the drive equipment, jackscrews or
shims.
d. Care shall be taken to prevent vertical jackscrews in the equipment feet from damaging the shimming surfaces.
e. Jackscrews shall be treated for rust resistance.
f. Jackscrews shall be supplied for leveling soleplates.
g. The vendor having unit responsibility shall supply all jackscrews.
h. Alternative methods of lifting equipment for the removal or insertion of shims or for moving equipment horizontally, such as
provision for the use of hydraulic jacks, may be proposed. Such arrangements shall be proposed for equipment that is too heavy to
be lifted or moved horizontally using jackscrews.
7.5.3.2 Anchor bolts shall not be used to fasten drive train equipment to mounting plates, or to fasten compressors through
baseplates or skids.
7.5.3.3 The vendor shall furnish stainless steel shim packs between the drive equipment feet and the mounting plates. The
alignment shims shall be in accordance with API 686, Chapter 7, and shall straddle the hold-down bolts and vertical jackscrews
and be at least 5 mm (1/4 in.) larger on all sides than the equipment feet.
7.5.3.4 Fasteners for attaching the components to the mounting plates shall be supplied by the vendor.
• 7.5.3.5
If specified, chock blocks shall be supplied by the vendor (see Annex L).
7.5.3.6 Anchor bolts shall be furnished by the purchaser, unless otherwise agreed upon. The vendor shall specify the
requirements for the anchor bolts.
7.5.3.7 The drive equipment feet shall be drilled with pilot holes that are accessible for use in final doweling.
7.5.3.8 Unless otherwise specified, epoxy grout shall be used for machines mounted on concrete foundations. The vendor shall
blast-clean in accordance with ISO 8501, Grade SA2 or SSPC SP6, all grout contact surfaces of the mounting plates and paint
those surfaces with inorganic zinc silicate primer in preparation for epoxy grout.
Note: Inorganic zinc silicate is compatible with epoxy grout, does not exhibit limited life after application (unlike most epoxy primers), and is
environmentally acceptable.
If specified, leveling plates shall be supplied. Leveling plates (see Annex L) shall be steel plates at least 19 mm (3/
• 7.5.3.9
4 in.) thick.
7.5.3.10 Equipment shall be designed for installation in accordance with API 686.
7.5.4 Baseplates and Skids
• 7.5.4.1
When a baseplate is specified, major equipment to be mounted on it shall be as specified by the purchaser. A baseplate
shall be a single fabricated steel unit, unless the purchaser and the vendor mutually agree that it may be fabricated in multiple
sections. Multiple-section baseplates shall have machined and doweled mating surfaces to ensure accurate field reassembly, and
provisions for a sufficient number of optical leveling targets to record and repeat the required level in the field.
Note: A baseplate may have to be fabricated in multiple sections because of shipping restrictions.
7.5.4.2 When a baseplate(s) is provided, it shall extend under the drive-train components so that any leakage from these
components is contained within the baseplate.
7.5.4.3 Baseplates shall be of welded construction. Abutting beams shall be welded on both sides. Flanges of load bearing
members shall not be spliced. Contact between webs at perpendicular joints shall be a minimum of one-third of the depth of the
smallest member.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
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7.5.4.4 The compressor crankcase, crosshead frame, cylinder supports and drive equipment shall be supported on load bearing
structural members.
7.5.4.5 Sufficient anchor bolt holes shall be provided to ensure that forces and moments are properly transmitted to the
foundation. Anchor points shall be located on internal and external load bearing structural members as necessary.
7.5.4.6 Baseplates shall be designed and built to adequately support the weight of the compressor, driver and accessories and to
avoid resonance with any possible excitation frequency. The baseplate shall be able to transmit all forces and moments generated
by the compressor and driver to the foundation.
7.5.4.7 The baseplate shall be provided with lifting lugs for at least a four-point lift. Lifting the baseplate complete with all
equipment mounted shall not permanently distort or otherwise damage the baseplate or the machinery mounted on it.
• 7.5.4.8
If specified, the baseplate shall be suitable for column mounting (i.e., shall have sufficient rigidity to be supported at
specified points) without continuous grouting under structural members. The purchaser and the vendor shall agree on the
baseplate design.
• 7.5.4.9
If specified, the baseplate shall be designed to facilitate the use of optical, laser based or other instruments for accurate
leveling in the field. The purchaser and vendor shall agree on the details of such provisions. When the requirements are met by
providing leveling pads and/or targets these shall be accessible with the baseplate on the foundation and the equipment mounted.
Removable protective covers shall be provided. For column mounted baseplates (see 7.5.2.8) leveling pads or targets shall be
located close to the support points. For non-column mounted baseplates, a pad or target should be located, as a minimum, at each
corner. When required for long units, additional pads shall be located at intermediate points.
7.5.4.10 The bottom of the baseplate between structural members shall be open. When the baseplate is installed on a concrete
foundation, accessibility shall be provided for grouting under all load bearing structural members. The members shall be shaped
to lock positively into the grout.
7.5.4.11 The underside mounting surfaces of the baseplate shall be in one plane to permit use of a single-level foundation.
When multi-section baseplates are provided, the mounting pads shall be in one plane after the baseplate sections are doweled and
bolted together.
7.5.4.13 Supports, braces and auxiliary equipment shall be mounted on load bearing structural members.
• 7.5.4.14
If specified, a dynamic analysis of the skid, including a modal analysis and forced response analysis shall be
performed. The modal analysis shall establish that mechanical natural frequencies of the baseplate are separated from the
significant excitation frequencies by at least 20%. The following loads, accounting for magnitude, phase, and frequency shall be
considered:
a. forces and moments due to reciprocating and rotating machinery;
b. acoustic-pulsation shaking forces in vessels and piping; and,
c. forces due to driver torque.
The forced response analysis shall demonstrate that the calculated vibration levels at any particular forcing frequency at any point
on the baseplate shall not exceed the following:
a. for a vibration frequency less than or equal to 10 Hz or less, a maximum displacement of 100 µm 0 – peak (4 mil 0 – peak)
(0.008 in peak-to-peak)
b. for a vibration frequency greater than 10 Hz, a maximum velocity of 4.5 mm/s RMS (0.175 in./s RMS)
If specified, a written report of the analysis shall be provided.
Note: This type of analysis is strongly recommended for equipment mounted offshore, platforms or equipment mounted on steel columns. For
equipment mounted on solid concrete foundations, dynamic skid analysis may be omitted.
• 7.5.4.15
If specified, sub-soleplates, complying with 7.5.3.3 shall be provided with the baseplate by the vendor.
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7.5.4.12 Unless otherwise specified, non-skid decking covering all walk and work areas shall be provided on the top of the
baseplate.
44
API STANDARD 618
7.5.5 Soleplates and Rails
When soleplates or rails are specified, they shall be provided by the vendor, and they shall meet the requirements of
• 7.5.5.1
7.5.3.1.1 and 7.5.3.1.2 in addition to those of 7.5.1.
Note: See Annex L for a typical sketch.
7.5.5.2 Adequate working clearance shall be provided at the bolting locations to allow the use of standard socket or box
wrenches and to allow the equipment to be moved using the horizontal and vertical jackscrews.
7.5.5.3 Soleplates shall be steel plates thick enough to transmit the expected loads from the equipment feet to the foundation
and to facilitate grouting. In no case shall they be less than 40 mm (11/2 in.) thick.
• 7.5.5.4
If specified, sub-soleplates shall be provided with the soleplates by the vendor.
7.5.5.5 When sub-soleplates are specified, they shall be steel plates at least 25 mm (1 in.) thick. The finish of the subsoleplates’ mating surfaces shall match that of the soleplates (see 7.5.1.5.2).
7.6 CONTROLS AND INSTRUMENTATION
7.6.1 General
7.6.1.1 Control systems, instrumentation, electrical systems, and their installation shall conform to the purchaser’s
specifications and unless otherwise specified, shall comply with the requirements of ISO 10438-1 (or equivalents such as API
614, Chapter 1), except as modified by the following clauses.
• 7.6.1.2
The vendor shall provide all auxiliary system instrumentation as specified.
7.6.1.3 All instrumentation furnished by the compressor manufacturer requires the purchaser’s review. Freestanding panels are
preferred. All instrumentation shall be securely supported to eliminate vibration and undue force on instrument piping and to
prevent damage during shipment, storage, operation and maintenance.
7.6.1.4 Some controls may be shipped loose for field installation in the purchaser’s piping as agreed between the purchaser and
the vendor. See 8.4.6 for shipment.
7.6.1.5 All tubing connections that must be dismantled for shipment shall have matched tags (initiation point, intermediate
sections and application point) attached by stainless steel wire.
7.6.2 Control Systems
• 7.6.2.1
The compressor can be controlled on the basis of inlet pressure, discharge pressure, flow, or some combination of these
parameters. This can be accomplished by suction throttling, valve unloaders, clearance pockets, speed variation, or a cooled
bypass from discharge to suction. The control system can be mechanical, pneumatic, hydraulic, electric or electronic, or any
combination thereof.
The following shall be as specified by the purchaser:
a. the type of control system (manual, automatic or programmable);
b. the control signal;
c. the control range;
d. the process sensing lines handling flammable, toxic, corrosive or high-temperature fluids that require transduced signals to the
instrumentation;
e. the source of the control signal and its sensitivity and range;
f. equipment to be furnished by the vendor;
g. speed of response required.
• 7.6.2.2
The configuration of the control system shall be Arrangement 1, 2 or 3, in accordance with ISO 10438-2 or API 614,
Chapter 2, as specified by the purchaser.
7.6.2.3 The vendor shall describe the complete control system (including alarms and shutdowns) in this scope of supply by
means of logic diagrams in accordance with IEC 60848. When the control system is supplied by others, the vendor shall provide
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
45
logic diagrams of the critical functions associated with the compressor operation (starting, stopping, capacity control, shutdowns
etc.).
• 7.6.2.4
The unloading arrangement for start-up and shutdown shall be stated on the data sheets and shall be agreed by the
purchaser and the vendor. If specified, automatic loading-delay interlock shall be provided to prevent automatic loaded starting. If
specified, automatic immediate unloading shall be supplied to permit re-acceleration of the motor after a temporary electric power
failure of an agreed maximum duration. The vendor and the purchaser shall agree on the modes and duration of unloaded and
partially loaded compressor operation. The vendor shall be responsible for the loading/unloading sequence.
7.6.2.5 Capacity control for constant-speed units will normally be achieved by suction valve unloading, clearance pockets, or
bypass (internal-plug type or external) or a combination of these methods. Step-less, reverse-flow capacity control acting on
suction valves shall be subject to purchaser’s approval. Control operation shall be either automatic or manual as specified on the
data sheet. Unless otherwise specified, five-step unloading shall provide nominal capacities of 100%, 75%, 50%, 25% and 0%;
three-step unloading shall provide nominal capacities of 100%, 50% and 0%, and two-step unloading shall provide capacities of
100% and 0%.
7.6.2.6 Capacity control on variable-speed units is usually accomplished by speed control, but this can be supplemented by one
or more of the control methods specified in 7.6.2.5.
Note: Reciprocating compressors are usually specified for constant-speed operation (see 6.1.10).
7.6.2.7 For variable speed control the speed of the compressor shall vary linearly with the control signal and an increase in
signal shall increase speed. Unless otherwise specified, the full range of the purchaser’s signal shall correspond to the required
operating range of the compressor for all specified operating conditions.
7.6.2.8 Unless otherwise specified, speed shall be adjustable by means of a hand speed changer.
7.6.2.9 Actuation of the control signal or failure of the signal or actuator shall neither prevent the governor from limiting the
speed to the maximum permissible nor prevent manual regulation with the hand speed changer.
7.6.2.10 Clearance pockets shall normally be of the fixed type (pocket either open or closed). The use of variable volume
clearance pockets requires purchaser’s approval. Each added clearance volume shall be included in the data sheets to indicate the
clearance it adds to the cylinder.
7.6.2.11 When a machine-mounted capacity control system is specified, the vendor shall provide a panel complete with
a. a positive-detent-type master selector device (one for each service on multi-service compressors) to provide the specified load
steps and,
b. indicators to show at which step the machine is operating.
7.6.3 Instrument and Control Panels
Interconnecting shop-fabricated piping, tubing and wiring for controls and instrumentation, when furnished and installed by the
vendor, shall be disassembled only as necessary for shipment.
7.6.4 Instrumentation
• 7.6.4.1
General
Instruments shall be furnished and mounted locally, on a gauge board, or on a panel, as specified.
• 7.6.4.2
Tachometers
If specified, a tachometer shall be provided for variable speed units. The purchaser shall specify the type, range, and indicator
provisions of the tachometer. Unless otherwise specified, the tachometer shall be supplied by the driver vendor and shall be
furnished with a minimum range of 0% – 125% of maximum continuous speed.
7.6.4.3 Temperature Measurement
7.6.4.3.1 Dial type temperature gauges shall be heavy duty and corrosion resistant. They shall be at least 125 mm (5 in.)
diameter, bimetallic liquid filled types and, unless otherwise agreed, shall have black marking on a white background.
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46
API STANDARD 618
7.6.4.3.2 A heat transfer compound shall be used between thermowells and sensing elements.
• 7.6.4.3.3
Packing or piston rod temperature indication, as recommended by the vendor, shall be provided for cylinders
operating at or above a gauge pressure of 35 bar (500 psig) and for all cylinders with liquid cooled packing (see 6.13.2.1). The
vendor shall supply thermocouples or resistance temperature detectors (RTD), as specified.
Note: See 7.6.8.1 for temperature monitoring systems.
• 7.6.4.3.4
If specified, main bearing and/or valve temperature detectors shall be supplied. Details of the monitoring
requirements and auxiliary equipment to be furnished (thermocouples, resistance temperature detectors (RTD), intrinsically safe
systems, etc.) shall be jointly agreed to by the purchaser and the vendor.
Note: See 7.6.8 for temperature monitoring systems.
7.6.5 Relief Valves
Relief valves shall be set to operate at not more than the maximum allowable working pressure, but not less than the values listed
in Table 4.
Rated Discharge Gauge Pressure
(Each Stage)
Minimum Relief Valve Set Pressure
Margin above Rated Discharge
Gauge Pressure
bar
psig
<10
<150
1 bar (15 psig)
>10 to 170
>150 to 2500
10%
>170 to 240
>2500 to 3500
8%
>240 to 345
>3500 to 5000
6%
>345
>5000
See footnote a
a For rated discharge gauge pressures above 345 bar (5000 psig), the relief valve setting shall be agreed on by the
purchaser and the vendor.
7.6.6 Alarms and Shutdowns
7.6.6.1 An alarm/shutdown system shall be provided. The alarm/shutdown system shall initiate an alarm if any one of the
specified parameters reaches an alarm point and shall initiate shutdown of the equipment if any one of the specified parameters
reaches the shutdown point.
7.6.6.2 The vendor shall provide the alarms and trips, as specified by the purchaser. Minimum requirements are listed in
Table 5.
7.6.6.3 The vendor shall advise the purchaser of any additional alarms and/or shutdowns considered essential to safeguard the
equipment.
• 7.6.6.4
The vendor shall supply the alarm and shutdown system to the extent specified.
Note: This can conveniently be achieved by the use of a responsibility matrix. See ISO 10438-1 (Annex C) or API 614, Chapter 1 (Appendix C),
for a typical responsibility matrix chart).
7.6.6.5 Transmitters (except vibration transmitters) shall be installed so that the vibration of the equipment will not cause the
transmitter to malfunction.
• 7.6.6.6
The purchaser shall specify whether alarm and shutdown circuits shall be designed to open (de-energize) or to close
(energize) to initiate alarms and shutdowns.
• 7.6.6.7
If specified, crossheads shall be equipped with a high crosshead-pin temperature alarm to protect the crosshead-pin
bushing.
Note: The system may consist of a spring-loaded eutectic device, which shall de-energize a pneumatic or hydraulic circuit on alarm.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Table 4—Relief Valve Settings
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
47
Table 5—Minimum Alarm and Shutdown Requirements
Condition
Alarm
Shutdown
High gas discharge temperature for each cylinder
X
X
Low frame lube-oil pressure
X
X
Low frame lube-oil level
X
—
Cylinder lubricator system failure
X
—
High oil-filter differential pressure
X
—
High frame vibration
X
X
High level in separator
X
X
Jacket coolant system failure
X
—
Note: The “X” indicates when the condition occurs, alarm or shutdown is required; “—” indicates when the condition occurs,
alarm or shutdown is not required.
7.6.7 Vibration and Position Detectors
The vendor shall furnish and mount a vibration detection and transducing device to provide the shutdown signal
• 7.6.7.1
required by 7.6.6.2. Each device shall have a velocity or accelerometer-type detector, and each shall provide for each of the
following functions:
a. continuous vibration measurement;
b. alarm;
c. shutdown.
The device and its mounting shall conform to API 670. Ball-and-seat or magnetic-type switches are unacceptable. If specified,
additional devices shall be provided. The purchaser and the vendor shall agree on the type, number, and location of the devices to
be mounted on the compressor frame (and on gear units, if applicable).
• 7.6.7.2
If specified, the vendor shall furnish and mount piston rod drop detectors of the non-contacting type to measure the
vertical movement of each piston rod (piston rod drop). If specified, a non-contacting device shall also be installed to measure
the horizontal movement of each piston rod. If a proximity-type probe is used for rod position indication, the probe and the
associated oscillator-demodulator and connecting cable shall be installed and calibrated in accordance with API 670. Unless
otherwise specified, each probe shall be mounted adjacent to the packing. Terminal boxes containing oscillator-demodulators
shall not be mounted on the compressor. If the piston rod is coated, calibration of the device shall make allowances for the
coating. See Annex C.
• 7.6.7.3
A one-event-per-revolution machined mark on the crankshaft shall be provided to permit synchronization on top dead
center with a cylinder performance analyzer and/or rod drop detector. If specified, or when a non-contacting device is installed to
indicate piston rod position, a corresponding phase-reference transducer(s) shall be provided. The transducer(s) shall be supplied,
installed and calibrated in accordance with API 670.
• 7.6.7.4
If specified, the vendor shall furnish and mount piston rod drop detectors of the contact type, such as a mechanical
roller or fuse metal plug (eutectic) type. The detail of the system shall be agreed between the vendor and the purchaser. Unless
otherwise specified, each detector shall be mounted on the packing gland. An inert gas, instrument air, or hydraulics shall be used
to pressurize the system. Diaphragm type pressure switches shall be used to sense loss of pressure.
• 7.6.8
Temperature Monitoring Systems
If specified, the vendor shall supply a temperature monitoring system installed and calibrated in accordance with API 670. The
temperatures monitored shall be as specified by the purchaser and may include but are not limited to:
a.
b.
c.
d.
main bearing temperatures;
valve temperatures;
packing temperatures;
crosshead pin bearing temperatures.
--``,,,``,,`````,``,,,
48
API STANDARD 618
7.7 PIPING AND APPURTENANCES
7.7.1 General
7.7.1.1 Piping and installation shall first conform to the purchaser’s specifications. Unless otherwise specified, in the absence
of purchaser specifications, piping shall comply with the requirements of ISO 10438-1 or API 614, Chapter 1, and ISO 10438-3
or API 614, Chapter 3, except as modified by the following clauses.
• 7.7.1.2
The extent of process and auxiliary piping to be supplied by the vendor shall be as specified by the purchaser.
7.7.1.3 If special flanges, not in accordance with the specified standards, are unavoidable at the purchaser connection, the
vendor shall supply a welding neck companion flange, bolting, and gasketing to be installed by others. The purchaser shall be
advised of this situation in the proposal.
Note: Cylinder connections are discussed in 6.8.4.
If specified, piping, pulsation suppression devices and knockout vessels at the initial and interstage suction points shall
• 7.7.1.4
have provisions for heat tracing and insulation.
Note 1: During certain atmospheric conditions, air can be at or close to saturated conditions; also, multi-stage air or hydrocarbon gas
compressors will usually have saturated conditions following intercooling.
Note 2: The user should ensure that the quantity of liquid carried into the inlet system is minimized and that any such carry-over does not collect
in the inlet system and form slugs.
Note 3: The design of a compressor inlet system for operation with a gas at or near saturation should consider the following factors:
—liquid separator close to the compressor suction;
—separator efficiency over the operating flow range;
—sufficient separator volume to handle incoming slugs;
—sufficient gas velocity in the line from the separator to the cylinder to minimize liquid dropout;
—elimination of low points between the separator and cylinder;
—slope of lines;
—insulation to minimize heat loss; and
—heat tracing to maintain the gas at or above the dew point.
7.7.1.5 The following items shall terminate with flanged connections at the edge of the base:
a. connections for interconnecting piping between equipment groupings, and off-base facilities,
b. connections for air, water, steam, and other utility services to a base area,
c. other purchaser connections.
Vendor-supplied piping systems shall terminate in flanged connections. Instrument tubing connections shall terminate in a flange
or a threaded connection in accordance with standard. Piping and component drains and vents shall terminate with a plugged or
blind-flanged valve, accessible from the edge of the base or from a work area. This is to keep work areas and walkways as free as
possible from obstructions. All piping supplied by the vendor shall be prefabricated. Any piping that cannot be shipped in the
assembled state shall be preserved, match marked and tagged to facilitate field assembly.
• 7.7.1.6
If specified, the vendor shall review drawings of all piping, appurtenances (pulsation suppression devices, intercoolers,
aftercoolers, separators, knockouts, air intake filters and expansion joints) and vessels immediately upstream and downstream of
the equipment and supports. The purchaser and the vendor shall agree on the scope and consequences of this review.
7.7.1.7 Internals of piping and appurtenances shall be accessible through openings or by dismantling for complete visual
inspection and cleaning.
7.7.1.8 Connections DN 40 (11/2 NPS) and smaller shall be designed to minimize overhung weight. Connections shall be
forged fittings or shall be braced back to the main pipe in at least two planes to avoid breakage due to pulsation-induced vibration.
Bracing shall be arranged to occupy minimum space.
Note 1: Slip-on flanges are not used on piping and appurtenances around reciprocating compressors due to their insufficient fatigue life.
Note 2: The attention of the user of this standard is drawn to the possibility of hazardous situations arising from the incompatibility of ISO and
ANSI pipe thread standards.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
49
7.7.1.9 All pipe flanges mating with cast iron compressor flanges shall be flat faced and utilize full-faced gaskets.
Note: For the purposes of this clause the term compressor flanges does not include faced and studded bosses.
7.7.1.10 Threaded piping joints shall not be used for flammable or toxic fluids, unless otherwise agreed, in accordance with
6.8.4.1.5. Where threaded joints are permitted, they shall not be seal welded.
Note: Threaded joints are typically only allowed for connections to non-weldable materials such as cast iron, instruments, or locations that must
be disassembled for maintenance.
7.7.1.11 Control valves shall have flanged ends.
7.7.1.12 Except where ring type joints are required or specified, pipe flange gaskets shall be flat, asbestos-free material up to
and including ANSI Class 300 pressure ratings, and spiral wound gaskets for higher ratings. Spiral wound gaskets shall have
external centering rings and windings of austenitic stainless steel or other suitable corrosion resistant materials (Monel, Inconel
etc.) depending on the fluids handled.
Note: Flared tubing fittings are not recommended for reciprocating compressor applications.
Special requirements for piping, flanges, valves, and other appurtenances in services such as hydrogen, hydrogen
• 7.7.1.13
sulfide, or other toxic services, shall be specified by the purchaser.
7.7.1.14 Inert gas purge systems shall be stainless steel downstream of the filters.
7.7.1.15 All flanges shall be socket-weld or weld-neck flanges. Lap-joint or slip-on flanges shall not be used.
7.7.2.1 For lubricating oil piping systems (with its mounted appurtenances) located within the confines of the main unit base
area, the vendor shall supply a complete system, including any assembly (console) base and any packaged unit accessory. The
vendor shall provide interconnecting piping when auxiliary equipment is specified to be located immediately adjacent to the
compressor in the vendor’s recommended location (see 6.14.2 and 7.7.1.5).
7.7.2.2 The vendor shall specify the maximum piping distance between the main frame and any auxiliary oil console, and the
required elevation difference.
7.7.2.3 Unless otherwise specified, oil piping (with the exception of cast-in-frame lines or passages) and tubing, including
fittings, shall be stainless steel.
7.7.2.4 After fabrication, oil lines shall be thoroughly cleaned.
Heads of oil-actuated control valves shall be vented back to the reservoir. If specified, instrument sensing lines to
• 7.7.2.5
shutdown switches shall have a continuous through-flow of oil.
7.7.3 Forced-feed Lubricator Tubing
7.7.3.1 Oil feed lines from force-feed lubricators to cylinder and packing lubrication points shall be at least 6 mm (1/4 in.)
outside diameter with a minimum wall thickness of 1.5 mm (0.065 in.). Tubing shall be seamless austenitic stainless steel. Fittings
shall be austenitic stainless steel. See 6.14.3.1.7 for check valves.
Note: For high-pressure compressors, heavier wall thickness tubing can be required.
7.7.3.2 Tubing shall be run together where possible. When winterization is specified, the tubing shall stand off from the
machine to allow insulation.
7.7.4 Coolant Piping
7.7.4.1 Unless otherwise specified, the vendor shall supply piping with a single inlet and a single outlet connection on each
cylinder requiring cooling (see Figure G-1, Plan C).
7.7.4.2 Both the coolant inlet line and the coolant outlet line to each compressor cylinder shall be provided with an isolation
valve. A globe valve with union shall be provided on the main outlet line from each cylinder. A sight flow indicator shall be
installed in the common coolant outlet line from each cylinder. Where more than one coolant inlet and outlet point exists on a
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
7.7.2 Frame Lubrication Oil Piping
50
API STANDARD 618
cylinder, one sight flow indicator and a regulating globe valve shall be provided for each coolant outlet point on each cylinder.
Cylinder coolant piping shall be equipped with valved coolant vents and drains (see Figure G-1).
When the purchaser specifies the vendor to supply coolant piping on the compressor, the vendor shall supply a piping
• 7.7.4.3
system for all equipment mounted on the compressor or compressor base. The piping shall be arranged to provide a single inlet
connection and a single outlet connection for each water circuit operating at different inlet temperature levels and shall include a
coolant control valve and a flow indicator as noted in 7.7.4.2. Series-type circuits shall have the necessary valved bypasses to
provide temperature control.
7.7.4.4 Where a thermosyphon or a static cooling system is provided (see 6.8.3), the vendor shall furnish piping with a drain
valve at its lowest point and an expansion tank (complete with fill-and-vent connections and level indication) sized to prevent
overflow of coolant (see Figure G-2, Plans A and B). A thermometer is required for a thermosyphon system.
7.7.5 Instrument Piping
Initial connections for remote mounted pressure instruments shall comprise an isolation valve conforming to the same
requirements as the system to which it is connected. Beyond the initial isolation valve, piping or tubing not less than 10 mm (3/8
in.) outside diameter may be used. Where convenient, a common primary connection may be used for remotely mounted
instruments that measure the same pressure. Such common connections shall not be smaller than DN 15 (NPS 1/2) and separate
secondary isolation valves shall be provided for each instrument. Where a pressure gauge is to be used for testing pressure alarm
or shutdown switches, common connections are required for the pressure gauge and associated switches.
7.7.6 Process Piping
• 7.7.6.1
The vendor may be required to supply process piping to the extent and requirements specified by the purchaser. See
ISO 10438-1 or API 614, Chapter 1.
7.7.6.2 When compressor process inlet piping and pulsation suppression equipment are furnished by the vendor, provisions
shall be made for the insertion of temporary start-up screens just upstream of the suction pulsation suppression device. The design
of the piping system, the suction pulsation suppression device and the temporary start-up screens shall afford easy removal and
reinsertion of the screens without the necessity of pipe springing.
• 7.7.6.3
When the screens are supplied by the vendor, the design, location, and orientation of the screens shall be agreed by both
the purchaser and the vendor prior to manufacture or purchase.
• 7.7.6.4
If specified, the vendor shall supply the removable spool pieces that accommodate temporary start-up screens.
Sufficient pressure taps to allow monitoring of the pressure drop across the screen shall be provided.
7.7.7 Distance Piece Vent and Drain Piping
7.7.7.1 The vendor shall supply distance piece vent and drain piping to the extent and requirements specified.
7.7.7.2 Drain and vent piping serving individual cylinders shall not be less than DN 25 (NPS 1) or 20 mm (3/4 in.) outside
diameter if tubing is used. Drain and vent headers shall not be less than DN 50 (NPS 2). Vent connections in the packing case and
interconnecting tubing within a distance piece shall be of austenitic stainless steel and of at least 6 mm (1/4 in.) outside diameter
with a minimum wall thickness of 1.24 mm (0.049 in.). See Annex I for a typical distance piece vent and drain system.
7.8 INTERCOOLERS, AFTERCOOLERS, AND SEPARATORS
7.8.1 Intercoolers and Aftercoolers
• 7.8.1.1
If specified, the vendor shall furnish an intercooler between each compression stage.
Unless otherwise specified, intercoolers shall comply with ISO 10438-1 or API 614, Chapter 1.
• 7.8.1.2
If specified, aftercoolers shall be furnished by the vendor.
Unless otherwise specified, aftercoolers shall comply with ISO 10438-1 or API 614, Chapter 1.
Note: Intercooling and after cooling of gasses from reciprocating compressors present some unique phenomena to be considered in the design of
exchangers.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
51
Caution should be exercised regarding:
—whether the gas should be on the tube side or on the shell side; very small pressure pulsation levels multiplied by the larger areas of the pass
separation plates can possibly produce very high vibratory forces in the tube bundle;
—the use of shell side rupture discs, relief valves or similar devices;
—the use of air-cooled heat exchangers because of their susceptibility to pulsation-induced vibration in systems and structures;
—the susceptibility of heat exchangers and their supporting structures to pulsation-induced vibration. Mechanical natural frequencies should not
be coincident with pulsation frequencies in the heat exchanger systems.
7.8.1.3 Unless otherwise specified, the water side of heat exchangers shall be designed in accordance with 6.1.7.
7.8.1.4 The choice of water on the tube or shell side of shell and tube heat exchangers shall be agreed between the vendor and
purchaser, with due consideration to pulsations, pressure levels, corrosion and maintainability.
Note: The purchaser may specify that the vendor shall furnish the fabricated piping between the compressor stages and the intercoolers and
aftercoolers. See ISO 10438-1 or API 614, Chapter 1.
7.8.2 Separators
• 7.8.2.1
If specified, liquid separation and collection facilities in accordance with 7.8.2.2 through 7.8.2.8 shall be provided
upstream of the compressor, and after every intercooler.
Note: Intercooling may result in condensation. See 6.8.1.2 and 7.7.1.4 and associated notes.
7.8.2.2 The type of liquid separation device and whether it is to be arranged in a separate vessel, or integral with the pulsation
suppression device, or integral with the intercooler, shall be mutually agreed upon by the vendor and purchaser. In the case of
cylinders handling gases that are or can become saturated, appropriate means should be used, in addition to the integral moisture
removal section, to prevent liquid carry over into the compressor cylinder. Special attention should be paid to integral separators
in pulsation dampener devices to avoid mechanical vibration in the separator pack.
Note 1: Moisture removal sections of pulsation suppression devices have demonstrated a low separation efficiency when oscillating flow effects
were not considered.
Note 2: Drain sumps on pulsation suppression devices can lead to longer cylinder connection nozzles, and can result in high vibrations on the
drain sump instrumentation.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
7.8.2.3 The liquid separation device shall remove 99% of all droplets of 10 microns or larger. Pressure drop shall be as defined
in 7.9.2.6.3.1.
7.8.2.4 Integral moisture removal sections shall have a drain sump or boot extending below the device shell into which the
separated liquid is directed.
7.8.2.5 Unless otherwise agreed, the capacity of the sump or boot of an integral separator, or lower part of the separate
separation vessel, shall be sufficient to contain the maximum expected liquid flow from any specified operating condition for not
less than 15 minutes, without activating any alarm.
7.8.2.6 The liquid separation device shall be equipped with a drain connection of not less than DN 25 (1 NPS), gauge glass
connections, and a level shutdown switch connection. The connections shall be flanged and fitted with blinds.
• 7.8.2.7
If specified, an automatic drainage system shall be provided. For air or inert gas service, this automatic drainage system
may comprise a float-operated trap with a manual bypass. In all other cases, the drainage system shall comprise a separate level
control valve with a manual bypass, operated by a level controller of an agreed type.
• 7.8.2.8
If specified, the drain sump or boot or lower part of the separate separation vessel shall be provided with a level
indicator and alarm and shutdown devices. Where a high level alarm and a high level shutdown are specified, the capacity of the
vessel or boot between the levels shall be equivalent to the maximum expected liquid flow for not less than 5 minutes.
52
API STANDARD 618
7.9 PULSATION AND VIBRATION CONTROL
7.9.1 General
7.9.1.1 The objective of the requirements of this subclause is to avoid problems with
a.
b.
c.
d.
vibration,
performance,
reliability, and
flow measuring error caused by acoustical interaction between the compressor and the system in which it operates.
7.9.1.2 The basic techniques used for control of detrimental pulsations and vibrations are the following:
a. system design based on analysis of the interactive effects of pulsations and the attenuation requirements for satisfactory levels
of piping vibration, compressor performance, valve life, and operation of equipment sensitive to flow pulsation;
b. utilization of pulsation suppression devices such as: pulsation filters and attenuators; volume bottles, with or without internals;
choke tubes; orifice systems; and selected piping configurations;
c. mechanical restraint design; specifically including such things as: type, location, and number of pipe and equipment clamps
and supports.
Note: Completion of purchaser requirements for pulsation suppressors (data sheet page 4, lines 15 through 26, and pages 13 and 14) is essential
for the vendor to quote and fabricate these accessories.
• 7.9.2
Alternate Operating Conditions
Operation with alternative gases, alternative conditions of service, or alternative start-up conditions shall be as specified.
Pulsation suppression devices shall be mechanically suitable for all specified conditions and gases.
When a compressor is to be operated on two or more gases of dissimilar molecular weights (for example, hydrogen and nitrogen),
pulsation levels shall be optimized for the gas on which the unit must operate for the greater length of time.
Pulsation levels shall be reviewed for all specified alternative gases, operating conditions, and loading steps to assure that
pulsation levels will be acceptable under all operating conditions. By mutual agreement, the pulsation level criteria of 7.9.4.2.5.2
may be exceeded for alternative conditions, however, the other design criteria of 7.9.4.2.5.2 shall be met.
Note: For the purposes of screening the need for reviewing alternate gases, a significant gas change is one that results in either a 30% change in
the speed of sound, or a molar mass change in the ratio of 1.7:1.
7.9.3 Multiple Unit Additive Effects
• 7.9.3.1
The purchaser shall specify when the compressor is to be operated in conjunction with other compressor units and their
associated piping systems. In this case, the additive effect of pressure pulsations from multiple units shall be addressed. The scope
of the analysis shall be based on agreement between the purchaser and vendor. If the additive effect indicates a requirement for
modifications to an existing system to obtain acceptable pulsation levels, such modifications shall be based on agreement between
the purchaser and the vendor.
Note: In some cases it may be necessary to impose tighter limits for each new compressor than those defined in 7.9.4.2.5 in order for the
combined system to achieve acceptable pulsation levels.
For preliminary sizing, and, if specified, for Design Approach 1 (see 7.9.4.2.2), pulsation suppression devices shall
• 7.9.3.2
have minimum suction surge volume and minimum discharge surge volume (not taking into account liquid collection chambers),
as determined from Equations 3, 4 and 5, but in no case shall either volume be less than 0.03 m3 (1 ft3).
In SI units
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
kT
V s = 8.1 × PD ⎛ -------s⎞
⎝ M⎠
⎛ ⎞
V
V d = 1.6 ⎜ ----1-s⎟
⎜ --- ⎟
⎝ rk⎠
1
--4
(3)
(4)
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
53
Vs and Vd > 0.03
(5)
In USC units
kT
V s = 7 × PD ⎛ -------s⎞
⎝ M⎠
1
--4
⎛ ⎞
V
V d = 1.6 × ⎜ ----1-s⎟
⎜ --- ⎟
⎝ rk ⎠
Vs and Vd > 1.0
where
VS
is the minimum required suction surge volume in m3 (ft3);
Vd
is the minimum required discharge surge volume in m3 (ft3);
k
is the isentropic compression exponent at average operating gas pressure and temperature;
r
is the stage pressure ratio at cylinder flanges (absolute discharge pressure divided by absolute suction pressure);
TS
is the absolute suction temperature in K (°R);
M
is the molar mass;
PD
is the total net displaced volume per revolution of all compressor cylinders to be manifolded in the surge volume in
m3/r (ft3/r).
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
The internal diameter of the surge volume shall be based on the minimum surge volume overall length required to manifold the
compressor cylinders. For a single-cylinder surge volume, the ratio of surge volume length to internal diameter shall not exceed
4.0. The inside diameter of spherical volumes shall be calculated directly from the volumes determined by Equations 3, 4 and 5.
Equations 3, 4 and 5 are intended to ensure that reasonably sized pulsation suppression devices are included with the compressor
vendor’s proposal and should provide satisfactory sizes for most applications. In some instances, the sizes should be altered
according to the simulation analysis employed by Design Approaches 2 and 3. Sizing requirements can be substantially
influenced by operating parameters, interaction among elements of the overall system, and mechanical characteristics of the
compressor system. The magnitude of the effects of these factors cannot be accurately predicted at the outset.
Some compressor applications require the use of properly designed low-pass acoustic filters. A low-pass acoustic filter consists of
two volumes connected by a choke tube. The volumes can be made up of two separate suppressors or one suppressor with an
internal baffle. A procedure for preliminary sizing of low-pass acoustic filters is presented in Annex O. The design shall be
confirmed by an acoustic simulation.
7.9.4 Design and Documentation
7.9.4.1 Design Approach Selection
7.9.4.1.1 Unless otherwise specified, Table 6 shall be utilized to determine the Design Approach. For applications above an
absolute pressure of 350 bar (5000 psia), the purchaser and the vendor shall agree on the criteria for pulsation suppression.
Note: A detailed description of the three design approaches is given in 7.9.4.2.
• 7.9.4.1.2
The purchaser shall specify if the analysis is to be performed by the vendor or a third party. If a third party is selected
to perform the analysis, the compressor vendor shall provide the necessary information required for the third party vendor to
complete the analysis.
54
API STANDARD 618
7.9.4.2 Design Approaches
7.9.4.2.1 General
The design approach choices are:
a. Design Approach 1—Empirical Pulsation Suppression Device Sizing.
b. Design Approach 2—Acoustic Simulation and Piping Restraint Analysis.
c. Design Approach 3—Acoustic Simulation and Piping Restraint Analysis plus Mechanical Analysis (with Forced Mechanical
Response Analysis if necessary).
Unless otherwise specified, each design approach includes all of the elements of preceding approaches, unless superseded by
more comprehensive methods. Elements of the various design approaches are summarized in 7.9.4.2.2, 7.9.4.4, and 7.9.4.5.
Flowcharts detailing work processes for each Design Approach can be found in Annex M.
Table 6—Design Approach Selection
Kw/cyl < 55
(hp/cyl < 75)
55 < Kw/cyl < 220
(75 < hp/cyl < 300)
220 < Kw/cyl
(300 < hp/cyl)
1
2
2
2
2
3
2
3
3
3
3
3
P < 35 bar
(P < 500 psi)
35 bar < P < 70 bar
(500 psi < P < 1000 psi)
70 bar < P < 200 bar
(1000 psi < P < 3000 psi)
200 bar < P < 350 bar
(3000 psi < P < 5000 psi)
Note: API 688 provides a discussion of the different operating and mechanical parameters that should be taken into account when considering a
design approach different from that indicated by Table 6, especially if less analysis is contemplated.
7.9.4.2.2 Design Approach 1—Empirical Pulsation Suppression Device Sizing
Pulsation suppression devices shall be designed using proprietary and/or empirical analytical techniques to meet line side
pulsation levels required in 7.9.4.2.5.2.2.1, and the maximum pressure drop allowed in 7.9.4.2.5.3.1, based on the normal
operating condition. Acoustic simulation analysis is not performed when using this design approach.
7.9.4.2.3 Design Approach 2—Acoustic Simulation and Piping Restraint Analysis
7.9.4.2.3.1 General
Design Approach 2 is pulsation control through the use of pulsation suppression devices and proven acoustic techniques in
conjunction with mechanical analysis of pipe runs and anchoring systems (clamp design and spacing) to achieve control of
vibrational response. This approach includes the evaluation of acoustic interaction between the compressor, pulsation suppression
devices and associated piping, including pulsation effects on compressor performance and an evaluation of acoustic shaking
forces in the pulsation suppression devices. The evaluation is accomplished by modeling the compressor system and the piping
and then performing an acoustic simulation to determine the response.
7.9.4.2.3.2 Compressor System Model
Pulsation suppression devices (or dampers) are initially sized using Design Approach 1, and analyzed using acoustic simulation.
The compressor system model normally includes piston and valve kinematics, cylinder passages, pulsation suppression device(s)
and terminates at the line-side nozzle flange. This model is only used for the acoustic simulation. There is no mechanical
modeling of the compressor system to evaluate mechanical resonances in Design Approach 2.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Rated Power per Cylinder
Absolute Discharge Pressure
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
55
7.9.4.2.3.3 Piping System Model
For applications where the piping system is not defined, the acoustic simulation can be performed with the piping system initially
modeled with an infinite length, acoustically non-reflective line. The allowable design limits of 7.9.4.2.3.4 apply. This step is
called a pre-study and is also referred to as a “bottle check” or “damper check.” For applications where the piping system is
defined, the pre-study may be omitted. The piping model replaces the acoustically non-reflective line in the simulation model.
7.9.4.2.3.4 Pre-study
When the acoustic simulation is performed prior to completion of the piping system model, the maximum allowable pressure
pulsation level at the pulsation suppression device line-side nozzle flange shall be 80% of the allowable value defined by
Equation 8 for single pulsation suppression devices, and 70% of the allowable value defined by Equation 8 when two or more
pulsation suppression devices are attached to common piping.
Note: A single pulsation device means a device that is not connected to another by common piping. Examples include: a single cylinder first
stage suction device of a single unit; a single cylinder discharge pulsation device of a single unit; and, single unit first stage suction or final stage
discharge device that manifolds all the cylinders that generate pulsation in the particular piping system. Examples of two or more pulsation
suppression devices attached by common piping are: interstage devices (even with intercoolers); single units with multiple pulsation suppression
devices for first stage suction or for final stage discharge piping systems; and multiple units attached to common piping systems.
In order to meet contract delivery, all parties should cooperate to schedule the design of the pulsation suppression device, the
pulsation analysis, and piping design. Ordering components after the pre-study can facilitate the procurement of long delivery
components of the pulsation suppression devices such as end caps, nozzles and cylindrical sections. However, the final length,
nozzle orientation and need for vessel internals cannot be optimized until the piping system is added to the acoustic model.
Therefore, it should be noted, that if the pulsation suppression devices are fabricated prior to finalizing the piping configuration
the only remaining system design optimization methods available to the designer is the installation of orifices, piping
modifications, and stiffening of the piping system. This sometimes leads to the need to order different pulsation suppression
devices to provide an adequate system, with a consequent negative impact on schedule.
7.9.4.2.3.5 Acoustic Simulation
When the layout and sizing of the piping system is completed, an acoustic simulation of the complete system shall be performed
to confirm compliance with the requirements of 7.9.4.2.5 or to identify changes necessary to achieve compliance.
A mechanical review shall be performed using span and basic vessel mechanical natural frequency calculations to avoid
mechanical resonance. This review shall result in a table of various pipe sizes that indicates the maximum allowable span (based
on the maximum compressor operating speed) between piping supports as a function of pipe diameter, and the separation margin
requirements of 7.9.4.2.5.2.3.3.
Note 1: In the piping design, when clamps are used to avoid mechanical resonances, the thermal flexibility effects should also be considered.
Note 2: To accurately predict and avoid piping resonances, the supports and clamps must dynamically restrain the piping. Piping restraints are
only considered to be dynamically restraining when they have either enough mass or stiffness to enforce a vibration node at the restraint. This
requirement is difficult to achieve with overhead piping and/or the use of simple supports, hangers, and guides.
7.9.4.2.4 Design Approach 3—Acoustic Simulation and Piping Restraint Analysis Plus Mechanical
Analysis— (with Forced Mechanical Response Analysis if Necessary)
7.9.4.2.4.1 General
This approach is identical to Design Approach 2, with the addition of a mechanical analysis of the compressor cylinder,
compressor pulsation suppression devices and associated piping systems including interaction between acoustic and mechanical
system responses. Forced mechanical response is included when necessary. Both acoustic and mechanical methods are used to
arrive at the most efficient and cost effective plant design.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
7.9.4.2.3.6 Mechanical Review and Piping Restraint Analysis
56
API STANDARD 618
7.9.4.2.4.2 Step 3a—Mechanical Natural Frequency Analysis of the Compressor and Piping System to Avoid
Coincidence with Significant Shaking Forces
a. The starting point of the mechanical model is either the crankcase-to-foundation interface or the crosshead guide-to-crankcase
interface. For modeling accuracy, this location shall be relatively rigid when compared to the rest of the compressor mechanical
model and/or it shall be accurately described by a six degree of freedom spring. The compressor mechanical model end point is
the second pipe clamp on the suction and discharge piping moving away from the line side nozzles of the pulsation suppression
devices. The factors that can influence the accuracy of the model are discussed in more detail in API 688. If specified, this
modeling will also include an analysis of the stresses found in the pulsation suppression device internals in accordance with
7.9.5.1.22 and 7.9.5.1.23.
Note 1: The intent is to avoid mechanical resonance of the compressor cylinders, pulsation suppression devices, and piping system at
frequencies where high shaking forces also exist.
Note 2: In some cases the compressor frame, crosshead guides and cylinders, mounted on a concrete foundation, can be considered to be
relatively rigid, and can be modeled using rigid elements.
Note 3: The compressor and pulsation suppression device mechanical model was formerly known as the compressor manifold model.
b. An analysis of the compressor and piping system shall be done to predict the mechanical natural frequencies. The mechanical
and acoustic system shall be designed to meet the separation margin criteria of 7.9.4.2.5.3.2 and the shaking forces shall not
exceed the limits found in 7.9.4.2.5.2.3.
Note: Geometrically-complex areas of the system such as cylinders, distance pieces, crosshead guides, frames, pulsation suppression device
nozzles, and piping, where span calculations cannot be applied accurately, are analyzed to determine mechanical natural frequencies, usually
with vendor proprietary methods, shop measured data, or finite element methods; with the intent of avoiding mechanical resonances at
frequencies where significant shaking forces also exist
7.9.4.2.4.3 Step 3b1—Forced Mechanical Response Analysis of the Compressor Mechanical Model
When the excitation frequency separation margins or the shaking force amplitude guidelines for pulsation suppression devices
cannot be met, a forced-mechanical-response analysis of the compressor mechanical model to the pulsation-induced forces and
cylinder-gas forces shall be performed. The allowable cyclic stress criteria in 7.9.4.2.5.2.5 shall apply. The compressor vendor
shall supply the allowable vibration limits for compressor components such as cylinders, distance pieces and crankcases.
Note: The allowable compressor vibration levels are generally the limiting design criteria. This analysis predicts the cyclic stress in the pulsation
suppression devices and associated piping. It is not intended that analysis of the cyclic stresses in the compressor components be included in this
design approach. The compressor components are included in the model only for the purpose of enabling the analysis of the effects of their
flexibility and dynamic movement on the pulsation suppression devices. The compressor manufacturer is expected to provide vibration criteria
to ensure that no fatigue failures or premature wear of compressor components occur, in accordance with 6.1.1.
7.9.4.2.4.4 Step 3b2—Forced Mechanical Response of the Piping System
When the excitation frequency separation margins or the shaking force amplitude guidelines for the piping system cannot be met,
a forced-mechanical response analysis of the piping system to acoustic shaking forces shall be performed. The allowable
vibration and cyclic stress limits in 7.9.4.2.5.2.4 and 7.9.4.2.5.2.5 respectively shall apply. The model end points shall be defined
by the analyst in agreement with the purchaser; in general, the piping system model should include all of the piping that was
included in the acoustic model. Factors that can influence the accuracy of the model are discussed in more detail in API 688.
When forced mechanical response analysis of the piping system is performed without doing a forced mechanical response
analysis of the compressor mechanical model, the starting point of the piping system is at the compressor cylinder flanges, which
are assumed to be rigid.
Note: As with Step 3b1, the vibration is generally the limiting design consideration, because when the vibration levels are within the
recommended allowable limits, the allowable stress levels are usually not approached. The exception is where high stress concentrations occur
at large diameter reductions such as nozzle connections and weldolets for small piping on significantly larger piping.
7.9.4.2.5 Design Criteria
7.9.4.2.5.1 General
Pulsation suppression devices and techniques applied in accordance with Design Approaches 1, 2, and 3 shall satisfy the basic
criteria in 7.9.4.2.5.2, and the other criteria in 7.9.4.2.5.3.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
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7.9.4.2.5.2 Basic Criteria
To evaluate compliance with the basic criteria, the following procedure applies:
1. Preliminary pulsation suppression device sizing. Determine pressure drop across the pulsation suppression device. The
criteria as described in 7.9.4.2.5.2.2.1 and 7.9.4.2.5.3.1 shall be met. Design Approach 1 is complete.
For Design Approaches 2 and 3:
2. Pre-study of pulsation suppression devices (if required). Determine pulsations at the compressor cylinder flanges, and at
the line side nozzle of the pulsation suppression device. The criteria as described in 7.9.4.2.5.3.1, 7.9.4.2.5.2.1, and
7.9.4.2.5.2.2.2 de-rated as in accordance with 7.9.4.2.3.4 shall be met. The criteria for pulsation suppression device nonresonant shaking force are described in 7.9.4.2.5.2.3.3.
3. After the layout of the piping system is completed, pulsation analysis of the complete pipe system is undertaken. The
criteria for maximum pressure drop and pulsations are given in 7.9.4.2.5.3.1, 7.9.4.2.5.2.1, and 7.9.4.2.5.2.2.2. The criteria for
pulsation suppression device non-resonant shaking forces are given in 7.9.4.2.5.3.3.
4. Specify maximum piping spans and determine vessel mechanical natural frequencies utilizing piping tables and basic
vessel calculations. The minimum allowable mechanical natural frequencies are given in 7.9.4.2.5.3.2.
If the criteria for Step 3 and Step 4 are met, Design Approach 2 analysis is complete. If the criteria under Steps 3 or 4 are not met
then either a redesign or, Steps 5 and 6 shall be performed:
5. Develop a mechanical model and determine mechanical natural frequencies; the minimum separation margins are in
7.9.4.2.5.3.2.
6. Determine the maximum allowable shaking forces in accordance with 7.9.4.2.5.2.3 and check whether these are higher
than the acoustic shaking forces calculated by acoustic simulation.
If the criteria for Step 5 and Step 6 are met, Design Approach 3 analysis is complete.
For the compressor system, if the criteria in Step 5 or Step 6 are not met, either a redesign or, Step 8 shall be performed.
For the piping system, if the criteria in Step 5 or Step 6 are not met, either a redesign or Step 7 shall be performed.
7. Determine pipe vibrations based on the maximum calculated acoustic shaking forces. Criteria for maximum allowable pipe
vibrations are in 7.9.4.2.5.2.4.
If the vibration criteria in Step 7 are not met, either a redesign or Step 8 shall be performed:
8. Calculate dynamic stresses in the compressor system or piping system, as required. Maximum allowable cyclic stresses are
in 7.9.4.2.5.2.5. For the compressor system, also compare the vibration levels calculated to those supplied by the compressor
vendor.
If the criteria for Step 7 or Step 8 are met, Design Approach 3 analysis is complete. If the criteria are not met, redesign is required.
Note: The calculations to determine the criteria for allowable shaking forces in Step 6 of this subclause may be omitted if the piping vibration
analysis is performed according to Step 7 directly after Step 5.
7.9.4.2.5.2.1 Maximum Allowable Compressor Cylinder Flange Pressure Pulsation
Unless other criteria (such as loss of compressor efficiency) are specified, the unfiltered peak-to-peak pulsation level at the
compressor cylinder flange, as a percentage of average absolute line pressure, shall be limited to the lesser of 7% or the value
computed from Equation 6.
P cf = 3R%
(6)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
If these criteria are met and Design Approach 2 is specified then Step 4 shall be performed. If Design Approach 3 is specified then
proceed directly to Step 5.
58
API STANDARD 618
where
Pcf
R
is the maximum allowable unfiltered peak-to-peak pulsation level, as a percentage of average absolute line pressure
at the compressor cylinder flange;
is the stage pressure ratio.
Note: Where maximum pulsation levels exceed these values and reasonable modifications are used, higher limits may be agreed on by the
purchaser and the compressor vendor.
Note 2: The frequencies, phase relationships, and amplitudes of pressure pulsation at the compressor valves can significantly affect compressor
performance and valve life. Pulsation levels measured at the compressor cylinder flange will usually not be the same as those levels existing at
the valves. Experience has shown, however, that pulsation limits at the cylinder flanges, as specified above, result in compressor performance
within the tolerances stated in this standard.
7.9.4.2.5.2.2 Maximum Allowable Pulsation Limits at and Beyond Line-side Nozzles of Pulsation
Suppression Devices
7.9.4.2.5.2.2.1 Pulsation suppression devices used in accordance with Design Approach 1 shall limit peak-to-peak pulsation
levels at the line side of the pulsation suppression device to a value determined by Equation 7.
In SI units
4.1
P 1 = ------------1 %
( PL )
--3
(7)
In USC units
10
P 1 = ------------1 %
( PL )
--3
where
P1
is the maximum allowable peak-to-peak pulsation level at any discrete frequency, expressed as a percentage of
average mean absolute pressure;
PL
is the average mean absolute line pressure, in bar (psia).
7.9.4.2.5.2.2.2 Unless otherwise specified, for Design Approaches 2 and 3, based on normal operating conditions, the peak-topeak pulsation levels in the initial suction, interstage and final discharge piping systems beyond pulsation suppression devices
shall satisfy the requirements specified in a and b.
a. For systems operating at absolute line pressures between 3.5 bar and 350 bar, (50 psia and 5000 psia), the peak-to-peak
pulsation level of each individual pulsation component shall be limited to that calculated by Equation 8.
In SI units
P1 =
400
a ⁄ ( 350 ) ⎛ ------------------------------------· ⎞
⎝
0.5 ⎠
( PL × DI × f )
In USC units
P1 =
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
300
-⎞
a ⁄ 1150 ⎛ --------------------------------⎝ ( P × D × f ) 0.5⎠
L
I
(8)
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59
where
P1
a
is the maximum allowable peak-to-peak level of individual pulsation components corresponding to the fundamental
and harmonic frequencies, expressed as a percentage of mean absolute line pressure;
is the speed of sound for the gas in m/s (ft/s);
PL
is the mean absolute line pressure in bar (psia);
DI
is the inside diameter of line pipe in mm (in.);
ƒ
is the pulsation frequency in Hz.
The pulsation frequency ƒ is derived from Equation 9.
N×z
f = -----------60
(9)
where
N
is the shaft speed in r/min;
z
is the 1, 2, 3,…, corresponding to the fundamental frequency and higher order frequencies.
b. For absolute pressures less than 3.5 bar (50 psia), the peak-to-peak levels of individual pulsation components need only meet
the levels calculated for an absolute pressure of 3.5 bar (50 psia).
Note: At pressures below 3.5 bar (50 psia) it is impractical to impose the stringent requirements of Equation 8.
7.9.4.2.5.2.2.3 When mutually agreed between the purchaser and vendor, the pulsation levels may exceed the limits defined
by 7.9.4.2.5.2, provided that requirements in 7.9.4.2.5.2.3 through 7.9.4.2.5.2.5 are satisfied, as noted in 7.9.4.2.5.2.1.
Note: The default design philosophy is based on minimizing pulsation and pressure drop utilizing proven acoustic control techniques. For
applications where the user may desire to relax the criteria, API 688 should be used as guidance to understand the risks and benefits that might
be encountered.
• 7.9.4.2.5.2.2.4
If specified, flow pulsations in systems which include elements sensitive to such phenomena shall be limited to
mutually agreed criteria, for example flow meters, check valves, and cyclone separators. Allowance for the presence of any such
sensitive elements outside the vendor’s scope of supply shall be as specified.
7.9.4.2.5.2.3 Maximum Allowable Acoustic Shaking Force
7.9.4.2.5.2.3.1 General
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
The maximum allowable non-resonant shaking force based on the design vibration guideline can be determined from Equation
10.
SF k = k eff × V
(10)
where
SFk
is the non-resonant shaking peak-to-peak force guideline relative to static structural stiffness in N (lbf);
keff
is the effective static stiffness along the piping or pulsation suppression device axis where the shaking force acts in
N/mm (lbf/in.). See Annex P for a detailed discussion of keff.
V
is the design vibration peak-to-peak guideline in mm (in.) (see Figure 4).
The shaking force guideline (SFk) applies to non-resonant vibration, therefore, shaking forces near resonance shall be reduced
well below the above shaking force guideline. This guideline is simplified from a complex analysis, contains many inherent
assumptions, and should be applied with care. See Annex P for conventions and a more detailed discussion of the maximum
allowable shaking forces.
Various support types provide ranges of support stiffness approximately as follows:
elevated un-braced tack supports
900 N/mm – 2700 N/mm
(5000 lbf/in. – 15,000 lbf/in.)
60
API STANDARD 618
grade level typical supports and clamps
2700 N/mm – 27,000 N/mm (15,000 lbf/in. – 150,000 lbf/in.)
grade level heavy supports and clamps
27000 N/mm – 45,000 N/mm (150,000 lbf/in. – 250,000 lbf/in.)
7.9.4.2.5.2.3.2 Maximum Allowable Piping System Non-resonant Acoustic Shaking Force
The maximum allowable piping non-resonant shaking forces shall be the lower of the values calculated from Equation 10 or from
Equation 11.
In SI units
SF pmax = 45 × NPS
(11)
In USC units
SFpmax = 250 × NPS
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
where
SFpmax
NPS
is the maximum piping non-resonant shaking peak-to-peak force guideline based on support strength N (lbf);
is the nominal pipe size in mm. (in.).
7.9.4.2.5.2.3.3 Maximum Allowable Cylinder Mounted Pulsation Suppression Device Non-resonant Shaking
Force
The maximum allowable non-resonant shaking forces for cylinder mounted pulsation suppression devices shall be the lower of the
values calculated from Equation 10 or from Equation 12. For Design Approach 2, since the shaking force levels are not evaluated
using Equation 10, the maximum allowable level shall be 10% of Equation 12. For frequencies within ±20% of the calculated
pulsation suppression device mechanical natural frequency, the maximum allowable level shall be 1% of Equation 12.
In SI units
SF dmax = 45000
(12)
In USC units
SFdmax = 10000
where
SFdmax
is the maximum pulsation suppression device non-resonant shaking peak-to-peak force guideline based on structural
strength in N (lbf).
Note: The shaking force criteria are intended as design criteria for shaking forces that act along the pulsation suppression device axis. Other
shaking forces that can be affected by the pulsation suppression device design such as (but not limited to) those acting parallel to the compressor
cylinder nozzles and those acting within the cylinder internal passages must also be evaluated. The evaluation criterion relative to the cylinder
varies and should be mutually agreed upon by the purchaser and compressor manufacturer.
7.9.4.2.5.2.4 Piping Design Vibration Criteria
The predicted piping vibration magnitude shall be limited to the design level in Figure 4. The diagram in Figure 4 is based on the
following:
a. a constant allowable vibration amplitude of 0.5 mm peak-to-peak (20 mils peak-to-peak) for frequencies below 10 Hz (the
frequency of 10 Hz is also according to ISO 10816);
b. a constant allowable vibration velocity of approximately 32 mm/s peak-to-peak (1.25 in./s peak-to-peak) for frequencies
between 10 and 200 Hz.
The limits in Figure 4 are intended as a design trigger point for analysis in accordance with 7.9.4.2.5.2.1. These values should not
be used as field acceptance criteria.
Note: The requirements in this subclause are considered to be conservative. There are however situations in which high stress risers and unbraced small diameter attached piping can pose a problem even though the main pipe exhibits acceptable vibration limits. There are no criteria
conservative enough to be used without a significant understanding of vibrational mechanics.
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61
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9LEUDWLRQ*XLGHOLQH LQFKHVSS
$3,'HVLJQ9LEUDWLRQ*XLGHOLQH
)UHTXHQF\ +]
Figure 4—Piping Design Vibration at Discrete Frequencies
7.9.4.2.5.2.5 Maximum Allowable Cyclic Stress
7.9.4.2.5.2.5.1 For Design Approach 3, Steps 3b1 and 3b2, pulsation and/or mechanically induced vibration shall not cause a
cyclic stress level in the piping and pulsation suppression devices in excess of the endurance limits of materials used for
components subject to these cyclic loads. For example, for carbon steel pipe with an operating temperature below 370°C (700°F),
the peak-to-peak cyclic stress range shall be less than 180 N/mm2 (26,000 psi) considering all stress concentration factors present
and with all other stresses within applicable code limits.
It is not considered necessary to demonstrate compliance with this clause for Design Approaches 1 and 2.
• 7.9.4.2.5.2.5.2
If specified, a piping system flexibility analysis that predicts forces and stresses resulting from thermal
gradients, thermal transients, pipe and fitting weights, static pressure, and bolt-up strains shall be performed. The specified piping
code shall provide the design criteria.
Modeling should include frame growth and component properties.
7.9.4.2.5.3 Other Criteria
7.9.4.2.5.3.1 Maximum Allowable Pressure Drop
For all design approaches:
a. Unless otherwise specified, the pressure drop for each operating case, based on steady flow through a pulsation suppression
device at the manufacturer’s rated capacity, shall not exceed 0.25% of average absolute line pressure at the device, or the value
determined by Equation 13, whichever is higher. These limits shall be increased by a factor of two when the pressure drop is
calculated using the total flow, where total flow is the sum of the steady flow plus dynamic flow components, provided that the
static component still meets the above criteria.
R–1
ΔP = 1.67 ⎛ ------------⎞ %
(13)
⎝ R ⎠
where
UP
R
is the maximum pressure drop based on steady flow through a pulsation suppression device expressed as a
percentage of mean absolute line pressure at the inlet of the device;
is the stage pressure ratio.
b. When a moisture separator is an integral part of the pulsation suppression device, the pressure drop for each operating case,
based on steady flow through such a device at the manufacturer’s rated capacity, shall not exceed 0.33% of the mean absolute line
pressure at the device, or the percentage determined by Equation 14, whichever is higher. These limits shall be increased by a
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
62
API STANDARD 618
factor of two when the pressure drop is calculated using the total flow, where total flow is the sum of the steady flow plus dynamic
flow components.
R–1
ΔP = 2.17 ⎛ ------------⎞ %
(14)
⎝ R ⎠
c. Pressure drops specified in this clause may be exceeded by mutual agreement between purchaser and vendor, when this is the
consequence of the preferred solution to piping resonance problems. The effects of dynamic interaction between compressor
cylinders, pulsation suppression devices and attached piping on cylinder performance are evaluated and pulsation-induced power
and capacity deviations are determined for the recommended design. This analysis should optimize pulsation related compressor
performance.
7.9.4.2.5.3.2 Separation Margins
Unless otherwise specified, both of the following guidelines are to be used together to avoid coincidence of excitation frequencies
with mechanical natural frequencies of the compressor, pulsation suppression devices and piping system.
a. The minimum mechanical natural frequency of any compressor or piping system element shall be designed to be greater than
2.4 times maximum rated speed.
Note 1: The intent is to be above twice running speed, because there is almost always sufficient excitation energy at the first and second orders
to excite resonances to a dangerous level.
Note 2: In certain compressor configurations, there can be significant excitation energy at higher orders of running speed and the system design
shall take this into account. When the minimum mechanical natural frequency guideline is not met or when there is significant excitation energy
at higher orders, the separation margins as defined in b) shall be maintained.
b. The predicted mechanical natural frequencies shall be designed to be separated from significant excitation frequencies by at
least 20%.
Note: The intent is that at least 10% separation for the actual system is achieved, and due to modeling limitations, if 20% is used for predicted
designs then 10% for the actual system will generally be attained.
Note 2: The ability to accurately predict resonance, and therefore separation margin, is greatly effected by the stiffness of the system. Elevated
rack-mounted piping systems will be inherently less stiff than grade-mounted pipe on concrete sleepers. In general, the stiffer the system, the
lower the sensitivity of the model to stiffness variability, and therefore the more accurate the prediction of the natural frequencies and avoidance
of coincidence with excitation frequencies.
7.9.4.2.5.3.3 Flow Measurement Error
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Unless otherwise specified, for flow meters located in the specified piping system, the maximum flow measurement error caused
by pulsation shall not exceed the following:
a. For Non-custody Transfer meters: 1.00% error.
b. For Custody Transfer meters: 0.125% error.
Note: See API 688 for a discussion on flow measurement error.
7.9.4.2.6 Documentation Requirements
A written report on the control of pulsation and vibration shall be furnished to the purchaser. Compliance with the requirements of
7.9 for the specified design approach shall be documented. The report shall define the analysis scope, including analysis
guidelines, compressor configuration, load steps, gas composition, and extent of the piping system analyzed. The report shall
include the recommendations resulting from the analysis. The documentation shall also present results applicable to each type of
analysis performed. Acoustic simulation results include cylinder nozzle and piping pulsation, acoustic shaking forces and flow
pulsation at equipment sensitive to this in spectrum form. Separation Margin analysis results includes natural frequencies and
mode shapes. Forced mechanical response results include vibration and cyclic stress. The format of the results presentation should
permit easy comparison with the analysis guidelines.
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63
7.9.5 Pulsation Suppression Devices
7.9.5.1 General
• 7.9.5.1.1
As a minimum, pulsation suppression equipment shall be designed and fabricated in accordance with the specified
pressure vessel code. If specified, the pulsation suppressors shall be stamped with the symbol as required by the specified pressure
vessel code (e.g. ASME Code) and registered with the required jurisdiction.
7.9.5.1.2 The maximum allowable working pressure for any component shall not be less than the set pressure of the relief
valve serving that component and, in any case, shall not be less than a gauge pressure of 4 bar (60 psig).
CAUTION: Purchasers should be aware of the overpressure hazards of closing suction block valves on idle compressors. Suctionside equipment between the block valve and the compressor cylinder should be rated for discharge pressure or have a protective
relief valve.
7.9.5.1.3 All materials in contact with process gases shall be compatible with the gases being handled. The corrosion
allowance for shells and internals of carbon-steel pulsation suppression equipment shall be a minimum of 3 mm (1/8 in.) unless
otherwise specified on the data sheet.
Regardless of materials, all shells, heads, baffles, and partitions shall have a minimum thickness of 10 mm (3/8 in.). Welding
procedures shall be provided (see Vendor Data section in Annex F, Item 17).
• 7.9.5.1.4
If specified, all butt welds shall be 100% radiographed.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
7.9.5.1.5 All flanged branch connections shall be reinforced so that the reinforcement provides a metal area equal to the cutaway area removed from the shell or head regardless of the metal thickness in the branch connection wall. Stress concentration
factors shall be considered to assure compliance with 7.9.4.2.5.2.5.
7.9.5.1.6 Suction pulsation suppression devices, not provided with an integral moisture removal section, shall be designed to
prevent trapping of liquid.
• 7.9.5.1.7
If specified, the suction pulsation suppression device(s) shall include a final moisture removal section as an integral
part of the vessel. This device shall be equipped as detailed in 7.8.
7.9.5.1.8 The nozzle length from the shell of the pulsation suppression device to the cylinder flange shall be held to a minimum
that is consistent with thermal flexibility and pulsation requirements. The nozzle area shall be at least equal to the area for the
nominal compressor cylinder flange size. Adequate space shall be allowed for access to and maintenance of the cylinder’s
working parts.
7.9.5.1.9 The orientation of the pulsation suppression devices and their nozzles shall be approved by the purchaser. Ratings,
types, and arrangements of all connections shall be agreed on by the purchaser and the vendor.
• 7.9.5.1.10
A DN 20 (3/4 NPS) pressure test connection shall be provided at each pulsation suppressor inlet and outlet nozzle.
An external drain connection of at least DN 25, (1 NPS) shall be provided for each compartment where practical. Where multiple
drains are impractical, circular notched openings in the baffles that are located at the low point of the vessel wall may be used with
the purchaser’s approval. The effect of such drain openings on the performance of the pulsation suppression device must be
considered. Arrangement of internals shall ensure that liquids will flow to drain connections under all operating conditions.
• 7.9.5.1.11
The cylinder nozzle of each discharge pulsation suppression device shall be provided with two connections located
to permit, without interference, the purchaser’s installation of thermowells of at least DN 25, (NPS 1) for a high-temperature
alarm or shutdown element and a dial thermometer. If specified, a thermowell connection of at least DN 25, (NPS 1) shall also be
provided for the cylinder nozzle of each suction pulsation suppressor.
7.9.5.1.12 Flanged connections DN 25, (NPS 1) and smaller, although reinforced in accordance with 7.9.5.1.5, shall be
designed to minimize overhung weight and shall be gusseted back to the main pipe or reinforcing pad in at least two planes to
avoid breakage resulting from vibration.
7.9.5.1.13 Unless otherwise specified, main connections to the compressor cylinder(s) and to process line shall be weld-neck
flanges. For non-standard connections, see 6.8.4.2.1 and 6.8.4.1.12.
7.9.5.1.14 Pulsation suppressors with an internal diameter equal to or greater than 450 mm (18 in.) shall have studded pad-type
inspection openings of at least 150 mm (6 in.) in diameter, complete with blind flanges and gaskets to provide access to each
64
API STANDARD 618
compartment. For pulsation suppressors with an internal diameter less than 450 mm (18 in.), 100 mm (4 in.) studded pad-type
inspection openings may be used. Inspection openings shall be located in a position that provides maximum visual inspection
capability of critical welds such as both sides of the baffles.
Note: For higher pressure flange ratings, the internal diameter of standard nozzles is less than the nominal sizes shown above. The purchaser
should determine if the actual size is adequate to accommodate inspection procedures.
7.9.5.1.15 Unless otherwise specified or approved by the purchaser, pulsation suppression device connections other than those
covered by 7.9.5.1.13 and 7.9.5.1.14 shall also be weld neck flanges. When threaded fittings are provided, they shall have a
minimum rating of Class 6000.
7.9.5.1.16 Flanges shall be in accordance with ISO 7005-1 or ASME B16.5; however, lap-joint and slip-on flanges shall
not be used. The finish of the gasket contact surface for flanged or machined bosses, other than the ring joint type shall be
between 3.2 µm and 6.4 µm (125 µin and 250 µin.) arithmetic average roughness (Ra). Either a serrated-concentric finish or a
serrated-spiral finish having a pitch in the range of 0.6 mm – 1.0 mm (24 grooves/in. – 40 grooves/in.) shall be used. The
surface finish of the gasket grooves of ring joint connections shall comply with ASME B16.5.
• 7.9.5.1.17
If specified, provisions shall be made for attaching insulation. All connections and nameplates shall be arranged to
clear the insulation.
7.9.5.1.18 All internals of pulsation suppression devices shall be designed, fabricated, and supported considering the
possibility of high acoustic shaking forces. Dished baffles in lieu of flat baffles shall be used. The same welding procedures as
applicable to external welds shall be followed. Full penetration welds shall be used for the attachment of the baffles to the
pulsation suppressor shell.
7.9.5.1.19 All butt welds shall be full penetration welds.
• 7.9.5.1.20
If specified, internal surfaces of carbon steel pulsation suppression devices shall be covered with a coating of
phenolic or vinyl resins that are suitable for the service conditions.
7.9.5.1.21 A stainless steel nameplate shall be provided on each pulsation suppression device. The manufacturer’s standard
data, purchaser’s equipment item number and purchase order number shall be included.
• 7.9.5.1.22
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If specified, the dynamic and static stresses on the pulsation suppression device internals that result from pulsationinduced shaking forces and pressure-induced static forces shall be analyzed to confirm compliance with 7.9.4.2.4.
7.9.5.1.23 If required by the specified pressure vessel code, such as ASME Section 8, Division 2, a low cycle fatigue analysis
shall be performed to predict the stresses from thermal gradients, thermal transients, and pressure cycles on the pulsation
suppression devices and internal components.
7.9.5.2 Fabrication and Thermally Induced Stresses in the Pulsation Suppression Device
7.9.5.2.1 Manufacturing tolerances and fit-up procedures for pulsation suppression devices, compressor cylinder nozzle
connections and line connections, shall be adequate to allow bolting of flanges without strain which may result in excessive
nozzle stresses, changes to component alignment or changes to rod runout. When two or more cylinders are to be connected to the
same pulsation suppression device, the flanges shall be fitted up to aligned cylinders at the compressor vendor’s shop and welded
in place to assure proper final alignment and to minimize residual stresses. This procedure is especially important for ring joint
flanges.
Note: An alignment fixture may be necessary on larger, block-mounted units.
7.9.5.2.2 The forces induced by thermal expansion of the pulsation suppression devices shall be taken into account to avoid
intolerable misalignment and excessive stresses during operation.
• 7.9.6
Supports for Pulsation Suppression Devices
If specified, supports for the pulsation suppression devices and vendor-supplied piping shall be furnished by the vendor. The
supports shall be designed considering static loading (including piping loads), acoustic shaking forces, and mechanical responses;
and shall not impose harmful stresses on the compressor, piping system, or pulsation suppression devices to which they are
attached. In calculating stress levels, the compressor frame growth and the flexibilities of the frame, crosshead guide, distance
piece, flange, and branch connection shall be considered. Compliant (resilient) supports having inherent vibratory dampening
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
65
characteristics are preferred as they accommodate thermal expansion. Loading of compliant supports shall be adjustable.
Noncompliant supports shall be designed to allow adjustment by the purchaser while in operation. Spring supports shall not be
used unless specifically approved by the purchaser.
Note: To the extent possible, the foundation of the supports should be integral with the compressor foundation. When noncompliant adjustable
supports are used, they should be adjusted by the purchaser at normal operating conditions.
7.10 AIR INTAKE FILTERS
• 7.10.1
For air compressors taking suction from the atmosphere, a dry-type air intake filter-silencer suitable for outdoor
mounting shall be provided by the vendor, unless otherwise specified. Special design details, if any, shall be as specified by the
purchaser. The vendor shall bring to the purchaser’s attention any hazards that he believes could result from complying with the
purchaser’s specification.
7.10.2 As a minimum, the following features shall be considered in the design of the filter-silencer:
a.
b.
c.
d.
e.
micron particle rating;
ease of cleaning during in-service conditions;
corrosion protection of filter and of internal surfaces of inlet piping;
avoidance of internal threaded fasteners;
connections for measuring pressure differential across the filter.
7.11 SPECIAL TOOLS
7.11.1 When special tools and fixtures are needed to disassemble, assemble or maintain the unit, they shall be included in the
quotation and furnished as part of the initial supply of the machine, together with complete instructions for their use. For multipleunit installation, the quantities of special tools and fixtures shall be agreed by the purchaser and the vendor. These or similar
special tools shall be used during shop assembly and post-test disassembly of the equipment.
• 7.11.2
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a.
b.
c.
d.
e.
Special tools for reciprocating compressors shall include, as a minimum:
mandrels for fitting solid wear bands on non-segmental pistons;
a lifting and lowering device for removal and insertion of valve assemblies with a mass greater than 15 kg (33 lb);
a crosshead removal and installation tool;
sleeve/cone to enable piston rod to be passed through completely assembled packing (see 6.13.1.7);
if specified, hydraulic tensioning tools.
7.11.3 When special tools are provided, they shall be packaged in separate, rugged metal box or boxes and marked “special
tools for (tag/item number).” Each tool shall be stamped or tagged to indicate its intended use.
7.11.4 All compressors shall be provided with suitable means of barring for maintenance. For compressors with a rated power
equal to or greater than 750 kW (1000 hp), and for compressors with a peak bar-over torque requirement equal to or greater than
1600 Newton-meters (1200 ft-lb), a power driven barring device shall be furnished. The vendor shall furnish a complete
description of the barring device including, such factors as method of operation (for example, manual engagement and automatic
disengagement on start of compressor), lockout signals required, location, guards and power required.
• 7.11.5
If specified, each compressor shall be fitted with a device to lock the shaft in position during maintenance. The device
shall allow locking of the shaft in multiple positions, as necessary for maintenance. The device shall be fitted with a limit switch.
Note: The purchaser should interlock this limit switch with the driver.
8 Inspection and Testing
8.1 GENERAL
8.1.1 The extent of the purchaser’s participation in the inspection and testing shall be as specified.
• 8.1.2
If specified, the purchaser's representative, the vendor's representative or both shall indicate compliance in accordance
with the inspector's checklist (Annex K) by initialing, dating and submitting the completed checklist to the purchaser before
shipment.
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API STANDARD 618
8.1.3 After advance notification to the vendor, the purchaser's representative shall have entry to all vendor and sub-vendor
plants where manufacturing, testing or inspection of the equipment is in progress.
8.1.4 The vendor shall notify sub-vendors of the purchaser's inspection and testing requirements.
8.1.5 The vendor shall provide sufficient advance notice to the purchaser before conducting any inspection or test that has been
specified to be witnessed or observed.
• 8.1.6
The amount of advanced notification required for a witnessed or observed inspection or test shall be as specified. Five
working days are usually considered adequate notice for inspections and tests. An observed test shall not be conducted until the
specified time.
Note: For an observed test, the purchaser should expect to be in the factory longer than is required for a witnessed test.
8.1.7 When shop inspection and testing have been specified, the purchaser and the vendor shall coordinate manufacturing hold
points and inspectors' visits.
8.1.8 Prior to a witnessed mechanical running or performance test, confirmation of the successful completion of the applicable
preliminary test shall be provided.
8.1.9 Equipment, materials and utilities for the specified inspections and tests shall be provided by the vendor.
8.1.10 The purchaser's representative shall have access to the vendor's quality program for review.
8.2 INSPECTION
8.2.1 General
•
a.
b.
c.
d.
e.
f.
g.
necessary or specified certification of materials, such as mill test reports;
test data and results to verify that the requirements of the specification have been met;
fully identified records of all heat treatment whether in the normal course of manufacture or as part of a repair procedure;
results of quality control tests and inspections;
details of all repairs;
if specified, final assembly maintenance and running clearances;
other data specified or required by applicable codes and regulations (see 5.2 and 9.3.1.1).
8.2.1.2 Pressure-containing parts shall not be painted until the specified inspection and testing of the parts is complete.
• 8.2.1.3
In addition to the requirements of 6.15.7.1, the purchaser may specify the following:
a. parts that shall be subjected to surface and subsurface examination;
b. the type of examination required, such as magnetic particle, liquid penetrant, radiographic and ultrasonic examination.
8.2.2 Material Inspection
8.2.2.1 General
• 8.2.2.1.1
When radiographic ultrasonic, magnetic particle or liquid penetrant inspection of welds or materials is required or
specified, the criteria in 8.2.2.2 through 8.2.2.5 shall apply unless other corresponding procedures and acceptance criteria have
been specified. Cast iron may be inspected only in accordance with 8.2.2.4 and/or 8.2.2.5. Welds, cast steel, and wrought material
shall be inspected in accordance with 8.2.2.2 through 8.2.2.5.
8.2.2.1.2 The vendor shall review the design of the equipment and impose more stringent criteria than the generalized limits
required in 8.2.2, if appropriate.
8.2.2.1.3 Defects that exceed the limits imposed in 8.2.2 shall be removed to meet the quality standards cited, as determined by
the inspection method specified.
Note: Care should be taken in the use of acceptance criteria for iron castings. Criteria developed for other materials are often not applicable.
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8.2.1.1 The vendor shall keep the following data available for at least 20 years:
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67
8.2.2.2 Radiography
8.2.2.2.1 Radiography shall be performed in accordance with ASTM E 94.
8.2.2.2.2 The acceptance standard used for welded fabrications shall be the specified pressure code or ASME Section VIII,
Division 1, UW-51 (for 100% radiography) and UW-52 (for spot radiography). The acceptance standard used for castings shall be
the specified pressure code or ASME Section VIII, Division 1, Appendix 7.
8.2.2.3 Ultrasonic Inspection
8.2.2.3.1 Ultrasonic inspection shall be in accordance with the specified pressure code or ASME Section V, Articles 5 and 23.
8.2.2.3.2 The acceptance standard used for welded fabrications shall be the specified pressure code or ASME Section VIII,
Division 1, Appendix 12. The acceptance standard used for castings shall be the specified pressure code or ASME Section VIII,
Division 1, Appendix 7.
The acceptance criteria for steel forgings shall be determined by the manufacturer in accordance with ASTM A 388M.
8.2.2.3.3 All crankshafts shall be ultrasonically tested in accordance with ASTM A 503 after machining, but before drilling.
8.2.2.4 Magnetic Particle Inspection
8.2.2.4.1 Both wet and dry methods of magnetic particle inspection shall be performed in accordance with ASTM E 709.
8.2.2.4.2 The acceptance standard used for welded fabrications shall be the specified pressure code or ASME Section VIII,
Division 1, Appendix 6 and Section V, Article 25. The acceptability of defects in castings shall be based on a comparison with the
photographs in ASTM E 125. For each type of defect, the degree of severity shall not exceed the limits specified in Table 7.
Table 7—Maximum Severity of Defects in Castings
Type
I
II
III
IV
V
VI
Defect
Linear discontinuities
Shrinkage
Inclusions
Chills and chaplets
Porosity
Welds
Maximum Severity Level
1
2
2
1
1
1
8.2.2.5 Liquid Penetrant Inspection
8.2.2.5.1 Liquid penetrant inspection shall be in accordance with the specified pressure code or with ASME Section V, Article
6 (see ASTM E 165).
8.2.2.5.2 The acceptance standard used for welded fabrications shall be the specified pressure code or ASME Section VIII,
Division 1, Appendix 8 and Section V, Article 24. The acceptance standard used for castings shall be the specified pressure code
or ASME Section VIII, Division 1, Appendix 7.
8.2.3 Mechanical Inspection
8.2.3.1 During assembly of the equipment, all components (including integrally cast-in passages and all piping and
appurtenances) shall be inspected to ensure they have been cleaned and are free of foreign materials, corrosion products and mill
scale.
• 8.2.3.2
When the oil system is specified to be run in the manufacturer’s shop, (see 6.14.2.1.10) it shall meet the test screen
cleanliness requirements specified in ISO 10438-1 or API 614, Chapter 1, and ISO 10438-3 or API 614, Chapter 3.
• 8.2.3.3
If specified, the purchaser may inspect the equipment and all piping and appurtenances for cleanliness before heads are
welded onto vessels, openings in vessels or exchangers are closed or piping is finally assembled.
• 8.2.3.4
If specified, the hardness of parts, welds and heat affected zones shall be verified as being within the allowable values
by testing. The method, extent, documentation and witnessing of the testing shall be mutually agreed by the purchaser and the
vendor.
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API STANDARD 618
8.2.3.5 Unless otherwise specified, the equipment components or surfaces subject to corrosion shall be coated with the
vendor’s standard rust preventive immediately after inspection. Temporary rust preventive shall be easily removable with
common petroleum solvents. The equipment shall be closed promptly upon the purchaser’s acceptance thereof. See 8.4.3 for
details.
8.3 TESTING
8.3.1 General
8.3.1.1 Equipment shall be tested in accordance with 8.3.2 and 8.3.3. Other tests that can be specified are described in 8.3.4.
8.3.1.2 At least six weeks before the first scheduled running test the vendor shall submit to the purchaser, for his review and
comment, detailed procedures for the mechanical running test and all specified running optional tests (8.3.4) including acceptance
criteria for all monitored parameters.
8.3.1.3 The vendor shall notify the purchaser not less than five working days before the date that the equipment will be ready
for testing. If the testing is rescheduled, the vendor shall notify the purchaser not less than 5 working days before the new test
date.
8.3.2 Hydrostatic and Gas Leakage Tests
8.3.2.1 Pressure-containing parts (including auxiliaries) shall be tested hydrostatically with liquid at a higher temperature than
the nil-ductility transition temperature of the material being tested and at the following minimum test pressures:
a. cylinder gas passages and bore: 11/2 times maximum allowable working pressure, but not less than a gauge pressure of 1.5 bar
(20 psig);
b. cylinder cooling jackets and packing cases: 11/2 times maximum allowable working pressure;
c. piping, pressure vessels, filters and other pressure-containing components: 11/2 times maximum allowable working pressure or
in accordance with the specified pressure code, but not less than a gauge pressure of 1.5 bar (20 psig).
The tests specified in Items a and b shall be performed prior to the installation of the cylinder liner.
Compressor cylinders shall be tested as assembled components using the heads, valve covers, clearance pockets, and fasteners to
be supplied with the finished cylinder.
Note: For gas pressure-containing parts, the hydrostatic test is a test of the mechanical integrity of the component and is not a valid gas leakage
test.
a. Pressure-containing parts such as compressor cylinders and clearance pockets handling gases with a molar mass equal to or
less than 12 or gases containing a mol percentage of H2S equal to or greater than 0.1%, shall undergo, in addition to the
hydrostatic test specified in 8.3.2.1, a pressure test with helium performed at the maximum allowable working pressure. Leak
detection shall be by helium probe or by submergence in water. The water shall be at a higher temperature than the nil-ductility
transition temperature of the material being tested. The internal pressure shall be maintained, while submerged, at the maximum
allowable working pressure. Zero leakage is required (see 8.3.2.6). In the case of testing by helium probe, the procedure, the
sensitivity of the instrument and the acceptance criteria shall be by prior agreement between the purchaser and the vendor.
b. Cylinders handling gases other than those described above in Item a shall undergo a gas leakage test as described in Item a,
with either air or nitrogen used as the test gas.
8.3.2.3 If the part tested is expected to operate at a temperature at which the strength of a material is below the strength of that
material at the testing temperature, the hydrostatic test pressure shall be multiplied by a factor obtained by dividing the allowable
working stress for the material at the testing temperature by that at the rated operating temperature. For piping, the stress values
used shall be those given in ASME B31.3. For vessels, the stress values used shall be those in the specified pressure code or in
ASME Section VIII, Division 1 for vessels. The pressure obtained from the aforementioned calculation shall then be used as the
minimum pressure at which the hydrostatic test is performed. The data sheets shall list actual hydrostatic test pressures.
Note: The applicability of this requirement to the material being tested should be verified before hydrostatic test, as the properties of many
grades of steel do not change appreciably at temperatures up to 200ºC (400ºF).
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8.3.2.2 The following gas test shall be performed to ensure that the components do not leak process gas. The leakage tests shall
be conducted with the components thoroughly dried and unpainted. Compressor cylinders shall be leak-tested without liners, but
with the following job components: heads, valve covers, clearance pockets and fasteners.
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69
8.3.2.4 Where applicable, tests shall be in accordance with the standard used to design the part. In the event that a discrepancy
exists between the test pressure in the standard used to design the part and the test pressure in this standard, the higher pressure
shall be used.
8.3.2.5 The chlorine content of liquids used to test austenitic stainless steel materials shall not exceed 50 ppm. To prevent
deposition of chlorides on austenitic stainless steel as a result of evaporative drying, all residual liquid shall be removed from
tested parts at the conclusion of the test.
Note: Chloride content is limited in order to prevent stress corrosion cracking.
8.3.2.6 Test duration shall be sufficient to allow complete examination of parts under pressure. The hydrostatic and gas leakage
tests shall be considered satisfactory when neither leaks nor seepage through the pressure containing parts or joints is observed for
a minimum of 30 minutes. Large, heavy pressure containing parts of complex systems can require a longer testing period to be
agreed upon by the purchaser and the vendor. Seepage past internal closures required for testing of segmented cases and operation
of a test pump to maintain pressure are acceptable.
8.3.2.7 Test gaskets shall be identical to those required for the service conditions.
8.3.3 Mechanical Running Test
8.3.3.1 All compressors, drivers, and gear units shall be shop tested in accordance with the vendor’s standard.
• 8.3.3.2
• 8.3.3.3
If specified, the shop test of the compressor shall comprise a 4-hour unloaded running test.
If specified, packaged units, including integral auxiliary system packages, shall undergo a 4-hour mechanical running
test prior to shipment. The test shall prove mechanical operation of all auxiliary equipment, as well as the compressor, reduction
gear, if any, and driver as a complete unit.
The compressor need not be pressure-loaded for this test. The procedure for this running test shall be agreed upon by the
purchaser and the vendor.
8.3.3.4 All oil pressures, viscosities, and temperatures shall be within the range of operating values recommended in the
vendor's operating instructions for the specific unit being tested.
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8.3.3.5 If replacement or modification of bearings, or dismantling to replace or modify other parts are required to correct
mechanical or performance deficiencies, the initial test shall be deemed not acceptable and the final shop tests shall be run after
these deficiencies are corrected.
• 8.3.3.6
Auxiliary equipment not integral with the unit, such as auxiliary oil pumps, oil coolers, filters, intercoolers and
aftercoolers need not be used for any compressor shop tests unless specified. If specified, auxiliary system consoles shall receive
both an operational test and a 4-hour mechanical running test prior to shipment. The procedure for this running test shall be as
agreed upon by the purchaser and the vendor.
• 8.3.3.7
The purchaser shall specify if dismantling for inspection (other than that required by evidence of malfunctioning during
testing) is required.
8.3.4 Other Tests
8.3.4.1 A bar-over test of the frame and cylinders shall be made in the vendor’s shop to verify piston end clearances and rod
runout. The final bar-over test shall be performed with all compressor cylinder valves in place to demonstrate no piston
interference. Vertical and horizontal piston-rod runout (cold) at packing case flanges shall also be measured during this test (see
6.3.1 and 6.10.4.6). Bar-over test results shall become a part of the purchaser’s records (Annex F, Item 59).
• 8.3.4.2
If specified, all machine-mounted equipment, prefabricated piping and appurtenances furnished by the vendor shall be
fitted and assembled in the vendor’s shop. The vendor shall be prepared to demonstrate that the equipment is free of harmful
strains.
8.3.4.3 All compressor suction and discharge cylinder valves shall be leak-tested in accordance with the vendor’s standard
procedure.
• 8.3.4.4
If specified, the compressor shall be subject to a performance test in accordance with ISO 1217 or the applicable ASME
power test code.
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API STANDARD 618
8.4 PREPARATION FOR SHIPMENT
Equipment shall be suitably prepared for the type of shipment specified, including blocking of the crankshaft. The
• 8.4.1
preparation shall make the equipment suitable for 6 months of outdoor storage from the time of shipment. If storage for a longer
period is specified, the purchaser will consult with the vendor regarding recommended procedures to be followed.
8.4.2 The vendor shall provide the purchaser with the instructions necessary to preserve the integrity of the storage preparation
after the equipment arrives at the job site and before start-up, as described in API 686, Chapter 3.
Note: It is recognized that failure to follow these instructions can jeopardize the successful operation of the equipment.
8.4.3 The equipment shall be prepared for shipment after all testing and inspection have been completed and the equipment has
been released by the purchaser. The preparation shall include provisions of 8.4.4 through 8.4.18.
8.4.4 Equipment shall be completely free of water prior to any shipment preparation.
8.4.5 Except for machined surfaces, all exterior surfaces that can corrode during shipment, storage or in service, shall be given
at least one coat of the manufacturer's standard paint. The paint shall not contain lead or chromates.
Note: Austenitic stainless steels are typically not painted.
8.4.6 Exterior machined surfaces, except for corrosion-resistant material, shall be coated with a rust preventive.
8.4.7 The interior of the equipment, including pulsation suppression devices, shall be clean; free from scale, welding spatter
and foreign objects; and sprayed or flushed with a suitable rust preventive that is oil soluble or can be removed with solvent. In
lieu of a soluble rust preventive, a permanently applied rust preventive may be used with prior approval by the purchaser.
8.4.8 Internal areas of frames, bearing housings, and oil system equipment such as reservoirs, vessels, and piping shall be
coated with an oil-soluble rust preventive or, with the purchaser’s prior approval, a permanent rust preventive.
8.4.9 Any paint exposed to lubricants shall be oil-resistant. When synthetic lubricants are used or specified (6.14.3.1.9), special
precautions shall be taken to ensure compatibility with the paint.
8.4.10 Flanged openings shall be provided with metal closures of a thickness equal to or greater than 5 mm (3/16 in.) with
elastomer gaskets and at least four full-diameter bolts. For studded openings, all nuts needed for the intended services shall be
used to secure closures. Each opening shall be car sealed so that the protective cover cannot be removed without the seal being
broken.
8.4.11 Threaded openings shall be provided with steel caps or round-head steel plugs in accordance with ASME B16.11. The
caps or plugs shall be of the same material as that of the pressure casing. Nonmetallic (such as plastic) caps or plugs shall not be
used.
8.4.12 Openings that have been beveled for welding shall be provided with closures designed to prevent the entrance of
moisture and foreign materials and damage to the bevel.
8.4.13 Lifting points and the center of gravity shall be clearly identified on the equipment package. The vendor shall
recommend the lifting arrangement.
• 8.4.14
The equipment shall be packed for domestic or export shipment as specified. Lifting, load-out and handling instructions
shall be securely attached to the exterior of the largest package in a well-marked weatherproof container. Where special lifting
devices, such as spreader bars, are required, the supply of these shall be subject to agreement. Upright position, lifting points,
weight and dimensions shall be clearly marked on each package.
8.4.15 The equipment shall be identified with item and serial numbers. Material shipped separately shall be identified with
securely affixed, corrosion-resistant metal tags indicating the item and serial number of the equipment for which it is intended.
Crated equipment shall be shipped with duplicate packing lists, one inside and one on the outside of the shipping container.
8.4.16 Any cylinders, heads, packing cases, packing, pistons, rods, crossheads and shoes, crosshead pins, bushings and
connecting rods that are dismantled for the purpose of separate shipment, or that are shipped as spare parts, shall be sprayed with
rust preventive, wrapped with moisture-proof sheeting and packed to prevent damage in shipment to, or storage at, the job site.
8.4.17 Exposed shafts and shaft couplings shall be wrapped with waterproof moldable waxed cloth or volatile-corrosioninhibitor paper. The seams shall be sealed with oil proof adhesive tape.
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71
8.4.18 Exterior surfaces of pulsation suppressors, piping and vessels shall be cleaned free of pipe scale, welding spatter and
other foreign objects.
Immediately after cleaning, external surfaces shall be painted with at least one coat of lead and chromate free primer.
8.4.19 Auxiliary piping connections furnished with the purchased equipment shall be impression stamped or permanently
tagged to agree with the vendor's connection table or general arrangement drawing. Service and connection designations shall be
indicated.
8.4.21 Component parts, loose parts and spare parts associated with a specific major item of equipment shall be individually
packed for shipment and shall not be mixed with similar parts associated with another major item of equipment. For example,
parts for the compressor shall not be packed together in the same crate with similar parts for the driver.
8.4.22 One copy of the manufacturer's installation instructions shall be packed and shipped with the equipment.
9 Vendor’s Data
9.1 GENERAL
9.1.1 VDDR Form
The information to be furnished by the vendor is specified in 9.2 and 9.3. The vendor shall complete and return the Vendor
Drawing and Data Requirements (VDDR) form (see Annex F) to the address(es) noted on the inquiry or order. This form shall
detail the schedule for transmission of drawings, curves, data and manuals as agreed to at the time of the proposal or order as well
as the number and type of copies required by the purchaser.
9.1.2 Data Identification
The data shall be identified on the transmittal (cover) letters and the title blocks or title pages with the following information:
a. purchaser/user’s corporate name;
b. job/project number;
c. equipment item number and service name;
d. inquiry or purchase order number;
e. any other identification specified in the inquiry or purchase order;
f. vendor’s identifying proposal number, shop order number, serial number or other reference required to completely identify
return correspondence.
9.1.3 Coordination Meeting
Unless otherwise agreed, a coordination meeting shall be held, preferably at the vendor’s plant, within 4 – 6 weeks after the
purchase commitment. The purchaser and vendor shall jointly agree on an agenda for this meeting which, as a minimum, shall
include the following items:
a.
b.
c.
d.
e.
f.
g.
h.
i.
j.
k.
purchase order, scope of supply and sub-vendor items (including spare parts);
review of applicable specifications and previously agreed exceptions to specifications;
data sheets;
compressor performance (including operating limitations);
pulsation suppression devices;
schematics and bills of material (for major items) of lube-oil systems, cooling systems, distance pieces and similar auxiliaries;
preliminary physical orientation of the equipment, piping and auxiliary systems;
drive arrangement and driver details;
instrumentation and controls;
scope and detail of pulsation and vibration analysis and control requirements (see Annexes M and N and 7.9.4.1);
identification of items for stress analysis review by purchaser (see 6.15.5.1);
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8.4.20 Bearing assemblies shall be fully protected from the entry of moisture and dirt. If volatile-corrosion-inhibitor crystals in
bags are installed in large cavities, the bags shall be attached in an accessible area for ease of removal. Where applicable, bags
shall be installed in wire cages attached to flanged covers and bag location shall be indicated by corrosion-resistant tags attached
with stainless steel wire.
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API STANDARD 618
l. inspection, expediting and testing reports;
m. details of functional testing;
n. other technical items;
o. start-up planning and training;
p. schedules for (1) transmittal of data, (2) production, (3) testing, and (4) delivery;
q. review details of vendor's quality control program.
9.2 PROPOSALS
9.2.1 General
The vendor shall forward the original proposal, with the specified number of copies, to the addressee specified in the inquiry
documents. The proposal shall include, as a minimum, the data specified in 9.2.2 through 9.2.4, and a specific statement that the
equipment and all its components and auxiliaries are in strict accordance with this standard. If the equipment or any of its
components or auxiliaries is not in strict accordance, the vendor shall include a list that details and explains each deviation. The
vendor shall provide sufficient detail to enable the purchaser to evaluate any proposed alternative designs. All correspondence
shall be clearly identified in accordance with 9.1.2.
9.2.2 Drawings
9.2.2.1 The drawings indicated on the Vendor Drawing and Data Requirements (VDDR) form (see Annex F) shall be included
in the proposal. As a minimum, the following shall be included.
a. A general arrangement or outline drawing for each machine train or skid-mounted package, showing overall dimensions,
maintenance clearance dimensions, overall weights, erection weights, and the largest maintenance weight for each item. The
direction of rotation and the size and location of major purchaser connections shall also be indicated.
b. Cross-sectional drawings showing the details of the proposed equipment.
c. Schematics of all auxiliary systems, including the lube-oil system, the cooling system, and the distance-piece vent-and-drain
system (when supplied). Auxiliary system schematic diagrams shall be marked to show which portions of the system are integral
with or mounted on the major equipment and which are separate.
d. Sketches showing methods of lifting the assembled machine or machines, packages, and major components and auxiliaries.
(This information may be included on the drawings specified in item a. above.)
9.2.3 Technical Data
The data described below shall be included.
a. Copies of the purchaser’s data sheets complete with the vendor’s information required for the proposal and literature to fully
describe details of the offering(s).
b. The noise data as required by the purchaser in the inquiry.
c. A copy of the Vendor Drawing and Data Requirements form (see Annex F) indicating the schedule according to which the
vendor agrees to furnish the data requested by the purchaser (see 9.3).
d. Net and maximum operating weights, maximum shipping and erection weights with identification of the item and the
maximum normal maintenance weight with identification of the item. These data shall be stated individually where separate
shipments, packages, or assemblies are involved. Approximate data shall be clearly identified as such. These data shall be entered
on the data sheets where applicable.
e. For a compressor with a variable-speed drive, the speed range over which the unit can be operated continuously under the
specified operating conditions.
f. The vendor shall specifically identify volumetric efficiency of the active end of any cylinder if it is less than 40% at any
specified operating condition.
Note: Performance predictions with volumetric efficiencies below 40% are often not reliable.
g. A schedule for shipment of the equipment in weeks after receipt of the order.
h. A list of major wearing components showing interchangeability with other purchaser units.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
9.2.2.2 If “typical” drawings, schematics and bills of material are used, they shall be marked up to show the weight and
dimension data to reflect the actual equipment and scope proposed.
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
•
•
73
i. A list of “start-up” spares, to include as a minimum, three lube-oil filter cartridge sets, plates and springs for each valve, one
set of packing rings for each rod, one set of rings and wear bands for each piston, plus all o-rings and gaskets necessary for a
complete change-out of all packing rings, all piston rings and all valves. The vendor shall add any items that his experience
indicates are likely to be required on start-up.
j. Complete tabulation of utility requirements, such as steam, water, electricity, air, gas and lube oil; including the quantity of
lube oil required and the supply pressure, the heat load to be removed by the oil and the nameplate power rating and operating
power requirements of auxiliary drivers. Approximate data shall be defined and clearly identified as such. This information shall
be entered on the data sheets.
k. A description of the tests and inspection procedures of materials in accordance with 8.2.2.
l. Complete details of any proposed air-cooled oil cooler.
m. A list of spare parts recommended that the purchaser should stock for normal maintenance purpose. (Any special requirements
for long term storage shall be as specified).
n. An itemized list of the special tools included in the offering.
o. A clear description of the metallurgy of all major components of the compressor (see 6.15.1.1 and 6.15.1.2).
p. A full description of the standard shop tests identified in 8.3. Special tests as specified shall also be fully described.
q. A list of relief valves, specifying those furnished by the vendor, as required by ISO 10438-1 or API 614, Chapter 1.
r. A description of the vendor’s intended response to any special requirements, such as those outlined in 6.7.1.
s. If specified, a list of similar machines installed and operating under analogous conditions to that proposed.
t. Any start-up, shutdown, or operating restrictions required to protect the integrity of the equipment.
u. An outline of all necessary special weather and winterizing protection required by the equipment, its auxiliaries and the driver
(if furnished by the vendor) for start-up, operation and idleness. The vendor shall list separately the protective items he proposes
to furnish.
v. Preliminary rod and gas load tabulation in accordance with 6.6.3.
9.2.4 Optional Tests
The vendor shall furnish an outline of the procedures to be used for each of the special or optional tests that have been specified,
or have been proposed by the vendor.
9.3 CONTRACT DATA
9.3.1 General
9.3.1.1 Contract data shall be furnished by the vendor in accordance with the agreed VDDR form.
9.3.1.2 Each drawing shall have a title block in the lower right-hand corner with the date of certification, identification data
specified in 9.1.2, revision number and data and title. Similar information shall be provided on all other documents including subvendor items.
• 9.3.1.3
The time allowed for the purchaser’s review of vendor’s data shall be as specified and agreed. Purchaser’s review of
vendor’s data shall not constitute permission to deviate from any requirements in the order unless specifically agreed upon in
writing. After the data have been reviewed and accepted, the vendor shall furnish certified copies in the quantities specified.
Note: The purchaser should promptly review the vendor's data upon receipt.
9.3.1.4 A complete list of vendor data shall be included with the first issue of major drawings. This list shall contain titles,
drawing numbers, and a schedule for transmittal of each item listed. This list shall cross-reference data with respect to the VDDR
form in Annex F.
9.3.2 Drawings
The drawing(s) furnished shall contain sufficient information so that when combined with the manuals covered in 9.3.7, the
purchaser can properly install, operate and maintain the ordered equipment. Drawings shall be clearly legible and reproducible.
(8-point minimum font size even if reduced from a larger size drawing). Drawings made specifically for the order shall be
identified in accordance with 9.1.2.
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74
API STANDARD 618
9.3.3 Performance Data
• 9.3.3.1
If specified, the vendor shall submit performance curves or tables of power and capacity versus suction pressure with
parameters of discharge pressure, showing the effects of unloading devices and showing any operating limitation and with
calculation input and output data identified, all as mutually agreed between the vendor and the purchaser.
9.3.3.2 Rod load and gas load charts for each load step, complete in accordance with 6.6, including inertial forces and rod
reversal magnitude and duration shall be furnished.
• 9.3.3.3
• 9.3.3.4
If specified, the vendor shall furnish the data required for independent rod load, gas load, and reversal calculations.
If specified, the effect of valve failure on rod loads and reversal shall be calculated and furnished. The required
specifics of this study shall be mutually agreed upon by the purchaser and vendor.
9.3.3.5 Curves of starting torque vs. speed shall be furnished for the compressor, for the motor at rated voltage and for the
motor at the specified voltage reduction. The curve sheet shall also state separately the (moment of inertia of the motor alone and
the resultant moment of inertia of the driven equipment referred to the motor shaft speed plus the calculated time for acceleration
to full speed at the specified voltages (see 7.1.2.) and specified operating conditions (see 7.1.1.6 and 7.1.2.1). All curves shall be
scaled in finite values. Values expressed in percentage terms alone shall not be provided.
9.3.4 Technical Data
Data shall be submitted in accordance with the VDDR form. The vendor shall provide full information to enable completion of
the data sheets, first “as purchased” and then “as built”. This shall be done by correcting and filling out the data sheets and
submitting copies.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
If any drawing comments or specification revisions lead to a change in the data, the vendor shall reissue data sheets. This will
result in reissue of the complete, corrected data sheets by the purchaser as part of the order specifications.
9.3.5 Progress Reports
The vendor shall submit progress reports to the purchaser at intervals specified.
Note: See the description of item 42 in Annex F for content of these reports.
9.3.6 Recommended Spares
9.3.6.1 The vendor shall submit complete parts lists for all equipment and accessories supplied. These lists shall include part
names, manufacturers’ unique part numbers, materials of construction (identified by applicable international standards). Each part
shall be completely identified and shown on appropriate cross-sectional, assembly-type cutaway or exploded-view isometric
drawings. Interchangeable parts shall be identified as such. Parts that have been modified from standard dimensions or finish to
satisfy specific performance requirements shall be uniquely identified by part number. Standard purchased items shall be
identified by the original manufacturer's name and part number.
9.3.6.2 The vendor shall indicate on each of these complete parts lists all those parts that are recommended as start-up or
maintenance spares, and the recommended stocking quantities of each. These should include spare parts recommendations from
sub-suppliers that were not available for inclusion in the vendor's original proposal
9.3.7 Installation, Operation, Maintenance and Technical Data Manuals
9.3.7.1 General
The vendor shall provide sufficient written instructions and all necessary drawings to enable the purchaser to install, operate, and
maintain all of the equipment covered by the purchase order. This information shall be compiled in a manual or manuals with a
cover sheet showing the information listed in 9.1.2, an index sheet, and a complete list of the enclosed drawings by title and
drawing number. The manual or manuals shall be prepared specifically for the equipment covered by the purchase order.
“Typical” manuals shall not be provided.
9.3.7.2 Installation Manual
All information required for the proper installation of the equipment shall be compiled in a manual that must be issued no later
than the time of issue of final certified drawings. The installation manual may be separate from the operating and maintenance
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
75
instructions. The installation manual shall contain information on alignment and grouting procedures, normal and maximum
utility requirements, centers of mass, rigging provisions and procedures, and all other installation data. All drawings and data
specified in 9.2.2 and 9.2.3 that are pertinent to proper installation shall be included as part of this manual (see description of line
item 64 in Annex F).
9.3.7.3 Operating and Maintenance Manuals
A manual containing all required operating and maintenance instructions shall be supplied no later than two weeks after all
specified tests have been successfully completed. In addition to covering operation at all specified process conditions, this manual
shall also contain separate sections covering operation under any specified extreme environmental conditions (see description of
line item 65 in Annex F).
9.3.7.4 Technical Data Manual
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
The vendor shall provide the purchaser with a technical data manual within 30 days of completion of shop testing (see description
of line item 66 in Annex F for minimum requirements of this manual).
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex A
(informative)
Data Sheets
77
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
ITEM NO.
Revision
JOB NO.
79
PURCHASE ORDER NO.
SPECIFICATION NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
1 APPLICABLE TO:
PROPOSALS
2 FOR/USER
3 NOTE:
PURCHASE
DATE
1
OF
BY
SERVICE
NO. WITH CYLS.
NO. REQ'D
BY MANUFACTURER
AFTER ORDER
TYPE MODEL NO(S)
6 COMPR.THROWS: TOTAL NO.
17
AS BUILT
BY MANUFACTURER
WITH PROPOSAL
5 COMPR. MFGR
7
PAGE
SITE/LOCATION
INDICATES INFO. TO BE
COMPLETED BY PURCH.
4
REVISION NO.
BY MANUFACTURER OR
PURCHASER AS APPLICABLE
SERIAL NO(S)
NOMINAL FRAME RATING
MAX/MIN ALLOWABLE SPEED
/
8 DRIVER MFGR.
BHP @ RATED R/MIN OF
r/min
DRIVER NAMEPLATE HP/OPERATING R/MIN
9 DRIVE SYSTEM:
DIRECT COUPLED
GEARED & COUPLED
10 TYPE OF DRIVER:
IND. MOTOR
11
CYLINDERS CONSTRUCTION:
SYN. MOTOR
/
V-BELT
STEAM TURBINE
GAS TURBINE
LUBE
NON-LUBE
ENGINE
OTHER
12
13
MAX ACCEPTABLE AVG PISTON SPEED
ft/min
OPERATING CONDITIONS (EACH MACHINE)
14
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
15
SERVICE OR ITEM NO.
16
STAGE
17
NORM. OR ALT. CONDITION
18
CERTIFIED PT. (X) MARK ONE
19
MOLECULAR WEIGHT
20
CP/CV (K) @ 150°F OR
°F
21
INLET CONDITIONS:
AT INLET TO:
22
NOTE:
23
PRESSURE (psia) @ PUL. SUPP. INLET
24
PRESSURE (psia) @ CYL. FLANGE
25
TEMPERATURE (°F)
26
REF: SIDE STREAM TEMPS (°F)
27
COMPRESSIBILITY (Zs )
28
INTERSTAGE:
29
ǻP BETWEEN STAGES, %/psi
INTERSTAGE ' P INCL:
30
DISCHARGE CONDITIONS:
31
PRESSURE (psia) @ CYL. FLANGE
32
PRESS. (psia) @ PUL. SUPP. OUTLET
33
TEMP., ADIABATIC, °F
34
TEMP., PREDICTED, °F
35
COMPRESSIBILITY (Z2 ) OR (ZAVG )
PULSE DEVICES
COMPRESSOR CYLINDER FLANGES
SIDE STREAM TO
STAGE(S), THESE INLET PRESS. ARE FIXED
PULSE DEVICES
AT OUTLET FROM:
PULSE DEVICE
PIPING
COOLERS
COMP. CYL. FLANGES
SEPARATORS
OTHER
36 * CAPACITY AT INLET TO COMPRESSOR, NO NEGATIVE TOLERANCE (-0%)
37
lb/h
CAPACITY SPECIFIED
38
39
IS
WET
DRY
MMSCFD/SCFM (14.7 psia & 60°F)
40 * MFGR.'S RATED CAPACITY (AT INLET TO COMPRESSSOR & BHP @ CERTIFIED TOLERANCE OF ±3% FOR CAP. & ±3% FOR BHP)
41
CAPACITY SPECIFIED
lb/h
42
IS
WET
DRY
43
INLET VOLUME FLOW (ICFM)
44
MMSCFD/SCFM (14.7 psia & 60°F)
45
BHP/STAGE
46
TOTAL BHP @ COMPRESSOR SHAFT
47
TOTAL HP INCLUDING
48
49
V-BELT & GEAR LOSSES
* CAPACITY FOR NNT
50
MANUFACTURER'S = REQUIRED ÷ 0.97
51
THEREFORE REQUIRED = MFR'S x 0.97
REMARKS:
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units)
OTHER
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
1
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
2
OF
17
BY
GAS ANALYSIS AT OPERATING CONDITIONS
MOLE % (BY VOLUME) ONLY
2
3
SERVICE/ITEM NO.
4
STAGE
5
NORMAL OR ALT
6
Revision
80
REMARKS
M.W.
7 AIR
28.966
8 OXYGEN
O2
9 NITROGEN
N2
28.016
10 WATER VAPOR
H2O
18.016
11 CARBON MONOX.
CO
28.010
12 CARBON DIOX.
CO2
44.010
13 HYDRO. SULFIDE
H2S
34.076
32.000
14 HYDROGEN
H2
2.016
15 METHANE
CH4
16.042
16 ETHYLENE
C2H4
28.052
17 ETHANE
C2H6
30.068
18 PROPYLENE
C3H6
42.078
19 PROPANE
C3H8
44.094
20 I-BUTANE
C4H10
58.120
21 n-BUTANE
C4H10
58.120
22 I-PENTANE
C5H12
72.146
23 n-PENTANE
C5H12
72.146
25 AMMONIA
NH3
17.031
INDUSTRY SERVICES
26 HYDRO. CHLOR.
HCI
36.461
NACE MR-O175 (6.15.1.11)
27 CHLORINE
Cl2
70.914
APPLICABLE SPECIFICATIONS
API 618-RECIPROCATING COMPRESSORS
FOR PETROLEUM, CHEMICAL AND GAS
24 HEXANE PLUS
28 CHLORIDES - TRACES
29
30
31
32
CALCULATED MOL WT.
33
Cp/Cv (K) @ 150° OR
°F
34 NOTE:
IF WATER VAPOR AND/OR CHLORIDES ARE PRESENT, EVEN MINUTE
35
TRACES, IN THE GAS BEING COMPRESSED, IT MUST BE INCLUDED ABOVE.
36
SITE/LOCATION CONDITIONS
37 ELEVATION
FT
BAROMETER
PSIA
AMBIENT TEMPS: MAX
38
MIN DESIGN METAL TEMP
°F (6.15.8.1)
39 COMPRESSOR LOCATION:
INDOOR
HEATED
UNHEATED
40
OUTDOOR
NO ROOF
UNDER ROOF
41
OFF-SHORE
42
WINTERIZATION REQUIRED
43 UNUSUAL CONDITIONS:
CORROSIVES
°F MIN
AT GRADE LEVEL
PARTIAL SIDES
WEATHER PROTECTION REQ.
DUST
FUMES
°F
RELATIVE HUMIDITY: MAX
%
MIN
%
ELEVATED:
PLATFORM:
ft
ON-SHORE
TROPICALIZATION REQ.
OTHER
44
45
ELECTRICAL CLASSIFICATIONS
46
HAZARDOUS
NON-HAZARDOUS
47 MAIN UNIT
CLASS
GROUP
DIVISION
48 L.O. CONSOLE
CLASS
GROUP
DIVISION
49 CW CONSOLE
CLASS
GROUP
DIVISION
50
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
1
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
3
OF
17
BY
PART LOAD OPERATING CONDITIONS
2 CAPACITY CONTROL
BY:
3
FOR:
4
WITH:
5
USING:
MFG'S CAP. CONTROL
PURCHASERS BY-PASS
BOTH
PART LOAD COND.
START-UP ONLY
BOTH
AUTO LOADING DELAY INTERLOCK (7.6.2.4)
FIXED VOLUME POCK.
6
ACTION:
7
NUMBER OF STEPS:
OTHER
AUTO IMMEDIATE UNLOADING
SUCTION VALVE UNLOADERS:
FINGER
PLUG
DIRECT (AIR-TO-UNLOAD)
ONE
OTHER
REVERSE (AIR-TO-LOAD/FAIL SAFE)
THREE
FIVE
OTHER
RAIN COVER REQUIRED OVER UNLOADERS
8
9
ALL UNLOADING STEPS BASIS MANUFACTURERS CAPACITY SHOWN ON PAGE 1.
10 INLET AND DISCHARGE PRESSURE ARE
AT CYLINDER FLANGES
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
11
SERVICE OR ITEM NO.
12
STAGE
13
NORMAL OR ALTERNATE CONDITION
14
PERCENT CAPACITY
15
WEIGHT FLOW, lb/h
16
MMSCFD/SCFM (14.7 psia & 60°F)
17
POCKETS/VALVES OPERATION *
18
POCKET CLEARANCE ADDED %
19
TYPE UNLOADERS, PLUG/FINGER
20
INLET TEMPERATURE, °F
21
INLET PRESSURE, psia
22
DISCHARGE PRESSURE, psia
23
DISCHARGE TEMP., ADIABATIC °F
24
DISCHARGE TEMP., PREDICTED °F
25
VOLUMETRIC EFF.,%HE/%CE
26
CALC. GAS ROD LOAD, lb, C **
27
CALC. GAS ROD LOAD, lb, T **
28
COMB. ROD LOAD, lb, C (GAS & INERTIA)
29
COMB. ROD LOAD, lb, T (GAS & INERTIA)
30
ROD REV., DEGREES MIN @ X-HD PIN ***
31
BHP/STAGE
32
TOTAL BHP @ COMPRESSOR SHAFT
33
TOTAL HP INCL. V-BELT & GEAR LOSSES
PULSATION SUPPRESSOR FLANGES
34
35
* SHOW OPERATION WITH THE FOLLOWING SYMBOLS:
36
37
HEAD END
38
OR
39
CRANK END
=
HE
=
CE
½
¾
¿
PLUS
40
­
°
®
°
¯
SUCTION VALVE(S) UNLOADED
=
S
=
F
=
V
OR
FIXED POCKET OPEN
OR
VARIABLE POCKET OPEN
41
42
EXAMPLE:
HE-F/CE-S = HEAD END FIXED POCKET OPEN / CRANK END SUCTION VALVE(S) UNLOADED.
43
* * C = COMPRESSION
44
MINIMUM PRESSURE REQUIRED TO OPERATE CYLINDER UNLOADING DEVICES,
45 CYLINDER UNLOADING MEDIUM:
46
T = TENSION
AIR
*** X - HD = CROSSHEAD
NITROGEN
PRESSURE AVAILABLE FOR CYLINDER UNLOADING DEVICES, MAX/MIN
psig
OTHER
/
81
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
psig
47 REMARKS, SPECIAL REQUIREMENTS, AND/OR SKETCH
48
49
50
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
4
OF
17
Revision
82
BY
SCOPE OF BASIC SUPPLY
1
2
PURCHASER TO FILL IN
3
DRIVER
(
(
) AFTER COMMODITY TO INDICATE:
):
BY COMPR. MFR.
BY PURCH.
VARIABLE SPEED
SPEED RANGE
r/min TO
r/min
4
INDUCTION MOTOR
SYNCHRONOUS MOTOR
STEAM TURBINE
ENGINE
5
API 541
API 546
API 611
API 612
6
OUTBOARD BEARING
7
SLIDE BASE FOR DRIVER (
8
MOTOR STARTING EQUIPMENT
9
GEAR (
10
COUPLING(S) (
11
):
)
)
LOW SPD.
API 613
HI-SPD.
API 677
QUILL SHAFT
KEY-LESS DRV.
KEY'D DRV.
OTHER
API 671
12
V-BELT DRIVE (
13
DRIVE GUARD(S) (
):
SHEAVES & V-BELTS (
):
)
MANUFACTURER'S STD.
14
15
(
); DEFINE
BASEPLATE FOR GEAR
):
OTHER
PROVISION FOR DRY AIR PURGE FOR OUTBOARD BEARING.
SOLE PLATE FOR DRIVER
(
BY OTHERS
STATIC CONDUCTING V-BELTS
NON-SPARKING
CALIF CODE
BANDED V-BELTS
API 671, ANNEX G
OTHER
PULSATION SUPPRESSORS
(
):
16
INITIAL INLET & FINAL DISCHARGE
SUPPORTS
(
)
INTERSTAGE
SUPPORTS
(
)
ALL INTERSTAGE INLET
17
SUPPRESSOR(S) TO HAVE MOISTURE REMOVAL SECTION:
INITIAL INLET
18
ACOUSTICAL SIMUL. STUDY
DESIGN
1,
EMPIRICAL PULSATION SUPRESSION DEVICE SIZING
19
APPROACH
2,
ACOUSTIC SIMULATION AND PIPING RESTRAINT ANALYSIS
20
CHECK ONLY ONE, SEE 7.9.4.1.1, TABLE 6)
3,
ACOUSTIC SIMULATION AND PIPING RESTRAINT ANALYSIS
(
):
PLUS MECHANICAL ANALYSIS
21 STUDY TO CONSIDER:
22
ALL SPECIFIED LOAD COND., INCL.
SINGLE ACT., PLUS
COMP.OPER.IN PARALLEL
ALTERNATE GASES
23
CRITICAL FLOW MEASUREMENT (7.9.4.2.5.3.3)
WITH EXISTING COMP. AND PIPING SYSTEMS
24
PULSATION SUPRESS'N DEVICE LOW CYCLE FATIGUE ANALYSIS
PIPING SYSTEM FLEXIBILITY
25
VENDOR REVIEW OF PURCHASER'S PIPING ARRANGEMENT
26 NOTE: SEE APPENDIX N FOR INFORMATION REQUIRED FOR STUDY
27
PACKAGED:
28
DIRECT GROUTED
29
RAILS
30
NO
YES
(
)
DEFINE BASIC SCOPE OF PACKAGING IN REMARKS SECTION, PAGE 5
CEMENTED/MORTAR GROUT
CHOCK BLOCKS
SHIMS
EPOXY GROUT; MFG/TYPE
BASEPLT.
SKID
SOLEPLT.
/
BOLTS OR STUDS FOR SOLEPLT. TO FRAME
SUITABLE FOR COLUMN MOUNTING (UNDER SKID AND/OR BASEPLATE)
31
LEVELING SCREWS
32
INTERCLR(S) (
33
SEPARATOR(S)
NON-SKID DECKING
)
(
SUB SOLEPLATES
OFF MOUNTED
MACHINE MTD.
AFTERCLR(S) (
)
)
CONDENSATE SEPARATION & COLLECTION FACILITY SYSTEM (7.8.2.1)
):
FINAL DISC. PIP. (
34
INTERSTAGE PIP. (
35
FLANGE FINISH
):
36
SPECIAL PIPING REQUIREMENTS (7.7.1.13). (DEFINE IN REMARKS SECTION NEXT PAGE)
37
INITIAL INLET,
38
INLET STRAINER(S)
39
MANIFOLD PIPING;
40
RELIEF VALVE(S) (
):
INITIAL INLET
41
RUPTURE DISC(S) (
)
THRU STUDS IN PIPING FLANGES
42
FOR ATMOSPHERIC INLET AIR COMPR. ONLY:
43
PREFERRED TYPE OF CYLINDER COOLING
API 618 FLANGE FINISH > 125 < 250 (7.9.5.1.16)
INTERSTAGE SUCTION PIPING ARR'D FOR:
(
):
INITIAL INLET
DRAINS
VENTS
INSULATION
(
)
SIDESTREAM INLET
AIR/GAS SUPPLY
INTERSTAGE
FINAL DISCHARGE
):
(
FORCED
HEAT TRACING
)
INLET FILTER -SILENCER
THERMOSYPHON
(
(
MANUFACTURER SHALL RECOMMEND
STATIC (STAND-PIPE)
45
BEST TYPE OF COOLING AFTER
CYL. COOLANT PIPING BY (
46
FINAL ENGINEERING REVIEW OF ALL
SINGLE INLET/OUTLET MANIFOLD & VALVES
47
OPERATING CONDITIONS
INDIVIDUAL INLET/ OUTLET PER CYL.
STAGE CYL'(S)
)
MATCH M'RKED
SIGHT GL'SS(ES)
VALVE(S)
CLOSED SYSTEM WITH PUMP, COOLER, SURGE TANK, & PIPING
49
50
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
)
STAGE CYL'(S)
44 NOTE:
48
SHOP FITTED
SPECIAL FINISH
SPOOL PIECE FOR INLET STRAINERS
RELIEF VALVES
INLET AIR FILTER
(
PARTIAL PRE FAB, FIELD FIT
FLANGE FINISH PER ANSI 16.5
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
SEPARATE COOLING CONSOLE (
):
DATE
PAGE
5
OF
17
BY
ONE FOR EA. UNIT
ONE CMMN TO ALL UNITS
DUAL PUMPS (AUX .& MAIN)
ARRANGED FOR HEATING JACKET WATER AS WELL AS COOLING
3
4
ROD PRESS. PACKING COOLING SYSTEM
5
FRAME LUBE OIL SYSTEM (
(
):
):
SEPARATE CONSOLE
AUX. PUMP
SHOP RUN
COMBINE WITH JKT SYSTEM
DUAL FILTERS WITH TRANSFER VALVE
FILTERS
SHOP RUN
CONTINUOUS FLOW IN SENSING LINE TO PRESSURE SWITCHES
6
7
ITEM NO.
REVISION
SCOPE OF BASIC SUPPLY (Con't)
1
2
JOB NO.
83
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
SEPARATE LUBE OIL CONSOLE (
):
EXTENDED TO MOTOR OUTBOARD BEARING
SHOP RUN
NOTE: PIPING BETWEEN ALL CONSOLES AND COMPRESSOR UNIT BY PURCHASER
8
SEE DATA SHEET PAGE 3 FOR DETAILS
IN INSTRUMENT & CONTROL PANEL
10
SEPARATE MACHINE MOUNTED PANEL
SEPARATE FREE STANDING PANEL
11
PNEUMATIC
HYDRAULIC
12
PROGRAMMABLE CONTROLLER
9
13
CAPACITY CONTROL (
):
INSTRUMENT & CONTROL PANEL (
ELECTRIC
):
ONE FOR EACH UNIT
14
15
BUFFER GAS CONTROL PANEL (
):
16
17
18
19
ELECTRONIC
ONE COMMON TO ALL UNITS
MACHINE MOUNTED
FREE STANDING (OFF UNIT)
ONE FOR EACH UNIT
ONE COMMON TO ALL UNITS
MACHINE MOUNTED
FREE STANDING (OFF UNIT)
SEE INSTRUMENTATION DATA SHEETS FOR DETAILS OF PANEL, ADDITIONAL REMARKS, AND INSTRUMENTATION.
NOTE:
ALL TUBING, WIRING, & CONNECTIONS BETWEEN OFF-UNIT FREE STANDING PANELS AND COMPRESSOR UNIT BY
PURCHASER.
20
21
HEATERS (
):
22
FRAME LUBE OIL
CYL. LUBRICATORS
ELECTRIC
STEAM
COOLING WATER
DRIVER(S)
GEAR OIL
23
24
BARRING DEVICE
25
CRANKCASE RAPID PRESSURE RELIEF DEVICE(S) (
(
):
MANUAL
26
SPECIAL CORROSION PROTECTION:
27
HYDRAULIC TENSIONING TOOLS
28
MECHANICAL RUN TEST:
NO
NO
NO
PNEUMATIC
ELECTRIC
FLYWHEEL LOCKING DEVICE
(
)
YES
MFR'S STANDARD
OTHER
YES
YES
MFG'S STANDARD
OTHER
COMPLETE SHOP RUN TEST OF ALL MACHINE MOUNTED EQUIPMENT, PIPING & APPURT.'(S)
29
30
31
PAINTING:
MANUFACTURER'S STANDARD
32
NAMEPLATES:
U.S. CUSTOMARY UNITS
33
SHIPMENT:
DOMESTIC
EXPORT
SPECIAL
SI UNITS
EXPORT BOXING REQUIRED
STANDARD 6 MONTH STORAGE PREPARATION
34
OUTDOOR STORAGE FOR OVER 6 MONTHS (
35
(
(
)
), PER SPEC
), PER SPEC
36
INITIAL INSTALLATION AND OPERATING TEMP ALIGNMENT CHECK AT JOBSITE BY VENDOR REPRESENTATIVE
37
COMPRESSOR MANUFACTURER'S USER'S LIST FOR SIMILAR SERVICE
38
COMPRESSOR VALVE DYNAMIC RESPONSE
39
PERFORMANCE DATA REQUIRED (9.3.3):
BHP VS. SUCTION PRESSURE CURVES
40
ROD LOAD/GAS LOAD CHARTS
41
VALVE FAILURE DATA CHARTED
SPEED/TORQUE CURVE DATA
42
43
BHP VS. CAPACITY PERFORMANCE CURVES OR TABLES REQUIRED FOR UNLOADING STEPS AND/OR VARIABLE
44
SUCTION/DISCHARGE PRESSURES
45
46
REMARKS:
47
48
49
50
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
)
--``,,,``,,`````,``,
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
6
OF
17
Revision
84
BY
UTILITY CONDITIONS
1
2 ELECTRICAL POWER:
AC VOLTS /
3
MAIN DRIVER
4
AUXILIARY MOTORS
5
HEATERS
PHASE
/
/
HERTZ
DC VOLTS
AC VOLTS
/
INSTRUMENT
/
/
ALARM & SHTDWN
/
/
/
PHASE
/
/
HERTZ
/
DC VOLTS
/
/
/
/
/
/
/
6
7
8 INSTRUMENT AIR:
NORMAL PRESSURE
psig
MAX/MIN
/
9 NITROGEN:
NORMAL PRESSURE
psig
MAX/MIN
/
FOR:
10 STEAM
DRIVERS
psig
psig
HEATERS
11 INLET: PRESS
psig
MAX/MIN
/
12 (NORM.) TEMP
°F
MAX/MIN
/
13 EXH'ST: PRESS
psig
MAX/MIN
/
14 (NORM.) TEMP
°F
MAX/MIN
/
FOR:
COMPRESSOR CYLINDERS
psig INLET: PRESS
°F
(NORM.) TEMP
psig EXH'ST:PRESS
°F
(NORM.) TEMP
psig
MAX/MIN
/
°F
MAX/MIN
/
psig
°F
psig
MAX/MIN
/
psig
°F
MAX/MIN
/
°F
psig
15
16
17 COOLING WATER
18
COOLERS
TYPE WATER
TYPE WATER
19 SUPP.: PRESS
psig
MAX/MIN
/
20 (NORM.) TEMP
°F
MAX/MIN
/
21 R'T'RN: PRESS
psig
MAX/MIN
/
22 (NORM.) TEMP
°F
MAX/MIN
/
psig SUPP.: PRESS
°F
(NORM.) TEMP
psig R'T'RN: PRESS
°F
(NORM.) TEMP
psig
MAX/MIN
/
°F
MAX/MIN
/
°F
psig
MAX/MIN
/
psig
°F
MAX/MIN
/
°F
23
24 COOLING FOR ROD PACKING:
25 TYPE FLUID
SUPPLY PRESS
26 FUEL GAS:
NORMAL PRESSURE
27
COMPOSITION
psig @
psig
°F
MAX/MIN
RETURN
psig @
/
psig
°F
LHV
BTU/ft
3
28
29 REMARKS/SPECIAL REQUIREMENTS:
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
7
OF
17
BY
CYLINDER DATA AT FULL LOAD CONDITION
1
2 SERVICE/ITEM NO.
3 STAGE
}
4 INLET PRESSURE, psia
5 DISCHARGE PRESSURE, psia
@ CYLINDER
FLANGES
6 CYLINDERS PER STAGE
7 SINGLE OR DOUBLE ACTING (SA OR DA)
8 BORE, in.
9 STROKE, in.
10 RPM:
RATED / MAX ALLOW
11 PISTON SPEED, ft/min:
RATED / MAX ALLOW
12 CYLINDER LINER, YES/NO
13 LINER NOMINAL THICKNESS, in.
3
14 PISTON DISPLACEMENT, ft /min
15 CYLINDER DESIGN CLEARANCE, % AVERAGE
16 VOLUMETRIC EFFICIENCY, % AVERAGE
17 VALVES, INLET/DISCHARGE, QTY PER CYL.
18 TYPE OF VALVES
19 VALVE LIFT, INLET/DISCHARGE, in.
20 VALVE VELOCITY, ft/min
21
SUCTION VALVE(S)
22
DISCHARGE VALVE(S)
23 ROD DIAMETER, in.
24 MAX ALLOW. COMBINED ROD LOADING, lb, C *
25 MAX ALLOW. COMBINED ROD LOADING, lb, T *
26 CALCULATED GAS ROD LOAD, lb, C *
27 CALCULATED GAS ROD LOAD, lb, T *
28 COMBINED ROD LOAD (GAS + INERTIA), lb, C *
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
29 COMBINED ROD LOAD (GAS + INERTIA), lb, T *
30 ROD REV., DEGREES MIN @ X-HD PIN**
31 RECIP WT. (PISTON, ROD, X-HD & NUTS), lb**
32 MAX ALLOW. WORKING PRESSURE, psig
33 MAX ALLOW. WORKING TEMPERATURE, °F
34 HYDROSTATIC TEST PRESSURE, psig
35 GAS LEAKAGE TEST PRESSURE, psig
36 INLET FLANGE SIZE/RATING
37
FACING
38 DISCHARGE FLANGE SIZE/RATING
39
FACING
40 DISCHARGE RELIEF VALVE SETTING DATA AT INLET PRESSURES GIVEN ABOVE:
41
RECOMMENDED SETTING, psig
42
GAS ROD LOAD, lb, C *
43
GAS ROD LOAD, lb, T *
44
COMBINED ROD LOAD, lb, C *
45
COMBINED ROD LOAD, lb, T *
46
ROD REVERSAL, °MIN @ X-HD PIN**
47 NOTE: CALCULATED AT INLET PRESSURES
48
GIVEN ABOVE & RECOMMENDED SETTING.
49
SETTLE-OUT GAS PRESSURE
50
(DATA REQUIRED FOR STARTING)
* C = COMPRESSION
* T = TENSION
85
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
**X-HD = CROSSHEAD
51 NOTES/REMARKS:
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
API STANDARD 618
RECIPROCATING COMPRESSOR
(API 618-5TH) DATA SHEET
U.S. CUSTOMARY UNITS
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
8
OF
17
Revision
86
BY
CONSTRUCTION FEATURES
1
2 SERVICE ITEM NO.
3 STAGE
4 CYLINDER SIZE (BORE DIA), in.
5 ROD RUN-OUT: NORMAL COLD VERTICAL
6
(per Annex C)
7 CYLINDER INDICATOR VALVES REQUIRED
8 INDICATOR CONNECTIONS ABOVE 5000 PSI
9 FLUOROCARBON SPRAYED CYLINDER
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
MATERIALS OF CONSTRUCTION
10 CYLINDER(S)
11 CYLINDER LINER(S)
12 PISTON(S)
13 PISTON RINGS
14 WEAR BANDS
REQUIRED
15 PISTON ROD(S): MATERIAL/YIELD, PSI
16 THREAD ROOT STRESS @ MACRL * @ X-HD END
17 PISTON ROD HARDNESS, BASE MATERIAL, Rc
18 PISTON ROD COATING
19
X REQUIRED
COATING HARDNESS, Rc
20 VALVE SEATS / SEAT PLATE
21 VALVE SEAT MIN HARDNESS, Rc
22 VALVE GUARDS (STOPS)
23 VALVE DISCS
24 VALVE SPRINGS
25 ROD PRESSURE PACKING RINGS
26 ROD PRESSURE PACKING CASE
27 ROD PRESSURE PACKING SPRINGS
28 SEAL / BUFFER PACKING, DISTANCE PIECE
29 SEAL / BUFFER PACKING, INTERMEDIATE
30 WIPER PACKING RINGS
31 MAIN JOURNAL BEARINGS, CRANKSHAFT
32 CONNECTING ROD BEARING, CRANKPIN
33 CONNECTING ROD BUSHING, X-HD END
34 CROSSHEAD (X-HD) PIN BUSHING
35 CROSSHEAD PIN
36 CROSSHEAD
37 CROSSHEAD SHOES
38 INSTRUMENTATION IN
COLD SIDE
39 CONTACT W/PROCESS GAS
HOT SIDE
40 * MACRL = MAXIMUM ALLOWABLE COMBINED ROD LOAD
41
FULL FLOATING PACKING
43
VENTED TO:
44
TYPE A
TYPE B
TYPE C
TYPE D
REF. FIGURE G-3
FLARE @
psig
SUCTION PRESSURE @
45
FORCED LUBRICATED
46
WATER COOLED,
47
OIL COOLED,
48
WATER FILTER
49
VENT/BUFFER GAS SEAL PACKING ARR.
ATMOS.
COVERS:
psig
CYLINDER COMPARTMENT:
(Outboard Distance Piece)
NON-LUBE
STAGE(S),
GPM REQ'D
STAGE(S),
GPM REQ'D
PROV.FUTURE WATER/OIL COOLING
50
CONSTANT OR
51
BUFFER GAS PRESSURE,
52
DISTANCE PIECE(S):
COMPRESSOR CYLINDER ROD PACKING
42
(REF. FIG I-1)
SOLID METAL
LOUVERED
psig
PURGED AT
psig
PRESSURIZED TO
psig
WITH RELIEF VALVE
FRAME COMPARTMENT:
(Inboard Distance Piece)
VARIABLE DISPOSAL SYSTEM
SPLASH GUARDS FOR WIPER PACKING
SCREEN
VENTED TO
psig
VENTED TO
psig
PURGED AT
psig
PRESSURIZED TO
psig
WITH RELIEF VALVE
DISTANCE PIECE MAWP
psig
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
JOB NO.
RECIPROCATING COMPRESSOR
(API 618-5TH) DATA SHEET
U.S. CUSTOMARY UNITS
ITEM NO.
REVISION NO.
PAGE
DATE
9
OF
17
BY
CONSTRUCTION FEATURES (CONTINUED)
1
2
FABRICATED CYLINDER, HEADS, & CONNECTION
3
SKETCHES FOR DESIGN REVIEW
OIL WIPER PACKING PURGE
4
BY PURCHASER. (6.15.5.13)
INTERMEDIATE PARTITION PURGE
BUFFER GAS PACKING ARR.
REF: ANNEX I
FIGURES I-1, I-2 & I-3
INERT BUFFER PURGE GAS:
5
N2
VENT, DRAIN, PURGE PIPING BY MFG'R
6
7
87
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
COUPLING(S)
LOW-SPEED
8
HI-SPEED
Between Compressor
& Driver or Gear
9
Between Driver &
Gear
V-BELT DRIVE
OTHER
NO
DRIVEN SHEAVE
YES
DRIVE SHEAVE
(COMPRESSOR SHAFT) (DRIVER SHAFT)
RPM (EXPECTED)
10
BY MANUFACTURER
PITCH DIA. (IN.)
11
MODEL
QTY & GROOVE X-SEC.
12
TYPE
POWER TRANSMITT'D
Incl. Belt Losses
13
14
API-671 APPLIES
YES
NO
15
INSPECTION AND SHOP TESTS (REF. 8.1.5)
16
REQ'D
17 *SHOP INSPECTION
DRIVER NAMEPLATE HP RATING
CENTER DISTANCE (IN.)
WITN. OBSER.
QTY, TYPE,
X-SEC., & LENGTH BELTS
18 ACTUAL RUNNING CLEARANCES
BELT SERVICE FACTOR (RELATIVE TO
19 AND RECORDS
DRIVER NAMEPLATE HP RATING)
20 MFG STANDARD SHOP TESTS
CYLINDER LUBRICATION
21 CYLINDER HYDROSTATIC TEST
NON-LUBE
STAGE(S)/SERVICE
22 CYLINDER PNEUMATIC TEST
LUBRICATED
STAGE(S)/SERVICE
23 CYLINDER HELIUM LEAK TEST
TYPE OF LUBE OIL:
SYNTHETIC
25 *MECHANICAL RUN TEST (4 HOUR)
LUBRICATOR
COMP. CRANKSHAFT, DIRECT
26 BAR-OVER TO CHECK ROD RUNOUT
DRIVE BY:
24 CYL. JACKET WATER HYDRO TEST
HYDROCARBON
CHAIN, FROM CRANKSHAFT
27 *LUBE OIL CONSOLE RUN/TEST (4 HOUR)
28 *COOLING H2O CONSOLE RUN/TEST
29 RADIOGRAPHY BUTT WELDS
30
GAS
OIL
ELECTRIC MOTOR
OTHER
LUBRICATOR MFR
FAB CYLS.
MODEL
31 MAG PARTICLE/LIQUID
TYPE LUBRICATOR:
SINGLE PLUNGER PER POINT
32
PENETRANT OF WELDS
33
SPECIFY ADDITIONAL
COMPARTM'T, TOTAL QTY.
34
REQUIREMENTS (8.2.1.3)
PLUNGERS (PUMPS), TOTAL QTY.
(6.14.3)
35
DIVIDER BLOCKS
SPARE PLUNGERS, QTY.
36 SHOP FIT-UP OF PULSATION SUPPL.
37
DEVICES & ALL ASSOCIATED
38
GAS PIPING
SPARE COMPARTM'T W/OUT PLUNGERS
HEATERS:
ELECTRIC W/THERM.(S)
STEAM
ESTIMATED WEIGHTS AND NOMINAL DIMENSIONS
39 *CLEANLINESS OF EQUIP., PIPING,
TOTAL COMPR. WT, LESS DRIVER & GEAR
lb
WT, OF COMPLETE UNIT, (LESS CONSOLES)
lb
41 *HARDNESS OF PARTS, WELDS &
MAXIMUM ERECTION WEIGHT
lb
42 HEAT AFFECTED ZONES
MAXIMUM MAINTENANCE WEIGHT
43 *NOTIFICATION TO PURCHASER OF
DRIVER WEIGHT/GEAR WEIGHT
/
lb
44 ANY REPAIRS TO MAJOR
LUBE OIL/COOLANT CONSOLE
/
lb
40
& APPURTENANCES
45 COMPONENTS
lb
FREE STANDING PANEL
46
SPACE REQUIREMENTS-FEET:
47
COMPLETE UNIT
48 *SPECIFIC REQUIREMENTS TO BE DEFINED,
49 FOR EXAMPLE, DISMANTLING, AUX EQUIPMENT
LUBE OIL CONSOLE
CYLINDER COOLANT CONSOLE
50 OPERATIONAL & RUN TESTS.
FREE STANDING PANEL
51 ANNEX K COMPLIANCE:
VENDOR
52
PURCHASER
LENGTH
WIDTH
HEIGHT
PISTON ROD REMOVAL DIST.
OTHER EQUIPMENT SHIPPED LOOSE (DEFINE)
53
PULSATION SUPP., WEIGHT
lb
54
PIPING
lb
55
INTERSTAGE EQUIPMENT
lb
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
JOB NO.
ITEM NO.
REVISION NO.
DATE
PAGE
10
OF
17
Revision
88
BY
UTILITY CONSUMPTION
1
2
ELECTRIC MOTORS
3
4
5
FOR INDUCTION
6
MOTORS SEE NOTE
7
OF 7.1.2.6 AND
8
MOTOR DATA SHEET
NAMEPLATE
LOCKED ROTOR
FULL LOAD
MAIN DRIVER NON-STEADY
HP
AMPS
STEADY STATE
STATE AMPS AT COMPRES-
AMPS
SOR RATED HORSEPOWER
(INDUCTION MOTORS ONLY)
9
MAIN DRIVER
10
MAIN LUBE OIL PUMP
@ COMPRESSOR RATED
AMPS
11
AUX LUBE OIL PUMP
HP OF
12
MAIN CYLINDER COOLANT PUMP
@ CURRENT PULSATIONS
13
AUX CYLINDER COOLANT PUMP
OF
14
MAIN ROD PKG COOLANT PUMP
15
AUX ROD PKG COOLANT PUMP
16
CYLINDER LUBRICATOR
%
17
18
19
ELECTRIC HEATERS
20
21
WATTS
22
FRAME OIL HEATER(S)
23
CYLINDER COOLANT HEATER(S)
24
CYL. LUBRICATOR HEATER(S)
25
MAIN DRIVER SPACE HEATER(S)
VOLTS
HERTZ
26
27
28
STEAM
29
30
FLOW
PRESSURE
TEMPERATURE
BACK PRESSURE
31
MAIN DRIVER
lb/h @
psig
°FTT TO
psig
32
FRAME OIL HEATER(S)
lb/h @
psig
°FTT TO
psig
33
CYL. LUB. HEATER(S)
lb/h @
psig
°FTT TO
psig
34
lb/h @
psig
°FTT TO
psig
35
lb/h @
psig
°FTT TO
psig
36
COOLING WATER REQUIREMENTS
37
38
FLOW
GPM
39
40
CYLINDER JACKETS
41
CYLINDER COOLANT CONSOLE
42
FRAME LUBE OIL COOLER
43
ROD PRESSURE PACKING*
44
PACKING COOLANT CONSOLE
45
INTERCOOLER(S)
46
AFTERCOOLER
INLET TEMP
°F
OUTLET TEMP
°F
INLET PRESS
psig
OUTLET PRESS
psig
MAX PRESS
psig
47
48
TOTAL QUANTITY, GPM
49 REMARKS/SPECIAL REQUIREMENTS:
50
*ROD PACKING COOLANT MAY BE OTHER THAN WATER
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
3
4
ITEM NO.
REVISION NO.
PAGE
DATE
11
OF
17
BY
FRAME LUBE OIL SYSTEM
1
2
89
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
SPLASH
BASIC LUBE OIL SYSTEM FOR FRAME:
REF: TYPE MAIN BEARINGS:
PRESSURE SYSTEM:
PRESSURE (FORCED)
TAP'RD ROLL'R
MAIN OIL PUMP DRIVEN BY:
5
HEATERS REQUIRED:
PRECISION SL'VE
ELEC. W/THERMOSTAT(S)
COMP. CRANKSHAFT
ELEC. MOTOR
PSV FOR MAIN PUMP EXTERNAL TO CRANKCASE
6
AUX OIL PUMP DRIVEN BY:
7
HAND OPERATED PRE-LUBE PUMP FOR STARTING
8
CHECK VALVE ON MAIN PUMP (FIG G-5)
ELEC. MOTOR
OTHER
OPERATIONAL TEST & 4 HOUR MECH RUN TEST
CONTINUOUS OIL FLOW THROUGH SWITCH SENSING LINE (7.7.2.5)
9
SEP. CONSOLE FOR PRESS. LUBE SYS:
ONE CONSOLE FOR EA. COMP.
10
Note:
CONSOLE TO BE OF DECK PLATE TYPE CONSTRUCTION SUITABLE FOR
MULTI-POINT SUPPORT AND GROUTING WITH GROUT & VENT HOLES.
11
12
13
14
Instrumentation to be listed on
Instrumentation Data Sheets.
ELECTRICAL CLASSIFICATION : CLASS
LUBE OIL
COMPRESSOR FRAME
17
DRIVER
,
DIV
COMPRESSORS
NON-HAZARDOUS
PRESSURE
psig
VISCOSITY
SSU @ 100°F
SSU @ 210°F
SUMP VOLUME
gal
GEAR
SYSTEM PRESSURES:
20
21
GROUP
FLOW
gpm
16
19
,
ONE CONSOLE FOR
BASIC SYS. REQ'MTS (NORM. OIL FLOWS & VOLUMES)
15
18
STEAM
OTHER
DESIGN
psig
HYDROTEST
PRESSURE CONTROL VALVE SETTING
CARBON
STEEL
PIPING MATERIALS:
22
23
UPSTREAM OF PUMPS & FILTERS
24
DOWNSTREAM OF FILTERS
psig
psig
STAINLESS STEEL
WITH SS FLANGES
PUMP REL'F VALVE(S) SET
psig
STAINLESS STEEL
WITH CARBON STEEL FLANGES
25
26
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
27
28
PUMPS
(Gear
or Screw Type Only)
29
MAIN
30
AUXILIARY
RAT'D FL'W
gpm
PRESSURE
psig
31
PUMP CASING MATERIAL (Ref. 6.14.2.1.5):
32
GUARD(S) REQ. FOR COUPLING(S):
33
DRIVER
HP
SPEED
r/min
MAIN PUMP
MECH. SEAL
REQ'D
AUX PUMP
MAIN PUMP
AUX PUMP
BY PURCH.
BY MFR.
WIRING TO TERMINAL BOX:
BY PURCH.
BY MFR.
35
SWITCHES
SHELL & TUBE
SINGLE
AUTOMATIC
GUARD TYPE OR CODE
ON-OFF-AUTO SEL. SWITCH:
COOLERS:
MANUAL
COUPLING
REQ'D
34
36
AUXILIARY PUMP CONTROL:
COLD START
REQ'D BHP
DUAL W/TRANSFER VALVE
MFG'S STD.
TEMA C
TEMA R (API 660)
37
REMOVABLE BUNDLE
38
W/BYPASS & TEMP CONTROL VALVE:
39
SEE SEPARATE HEAT EXCHANGER DATA SHEETS FOR DETAILS, SPECIFY % GLYCOL ON COOLING WATER SIDE
40
FILTER(S)
SINGLE
DESIGN PRESSURE,
42
MICRON RATING,
44
MANUFACTURER
AUTO
ASME CODE DESIGN
ǻP P CLEAN,
psig
ASME CODE STAMPED
psi
CARTRIDGE MATERIAL,
BONNET MATERIAL,
SYS. COMPONENT SUPP.
AIR COOLED W/AUTO TEMP CONTROL (API-661) Data Shts - Attached
MANUAL
DUAL W/TRANSFER VALVE
41
43
WATER COOLED
RTD'S/THERMOCOUPLES
CASING MATERIAL,
MODEL
ǻP COLLAPSE,
psi
CARTRIDGE P/N
FURN.SPARE CARTR.,QTY
MANUFACTURER
45
MAIN PUMP
OIL COOLER(S)
46
AUXILIARY PUMP
TRANSFER VALVE(S)
47
MECHANICAL SEALS
PUMP COUPLING(S)
48
ELECTRIC MOTORS
SUCTION STRAINER(S)
49
STEAM TURBINES
CHECK VALVE(S)
50
OIL FILTER(S)
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
MODEL
API STANDARD 618
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
PAGE
4
12
DATE
OF
17
BY
COOLANT SYSTEM
COMPRESSOR CYL.(S)
BASIC COOLING SYS. FOR:
3
5
ITEM NO.
REVISION NO.
1
2
ROD PACKING(S)
HEATERS REQ.'D FOR PRE-HEATING:
OPEN, PIPING BY:
PRESSURE FORCED CIRCULATING SYS:
PROCESS COOLER(S)
ELEC.,W/ THERMOSTAT(S)
PURCH.
MFR
MAIN COOLANT PUMP DRIVEN BY:
ELEC. MOTOR
STEAM TURBINE
OTHER
6
AUX COOLANT PUMP DRIVEN BY:
ELEC. MOTOR
STEAM TURBINE
OTHER
7
SEP. CONSOLE FOR COOLANT SYSTEM.:
8
NOTE:
9
10
11
Revision
90
ONE CONSOLE FOR EA. COMP.
Instrumentation to be listed on
instrumentation data sheets.
14
CYLINDER(S),
STAGE
15
CYLINDER(S),
STAGE
16
CYLINDER(S),
STAGE
17
CYLINDER(S),
STAGE
18
CYLINDER(S),
STAGE
19
CYLINDER(S),
STAGE
20
PISTON ROD PACK'G TOTAL
21
INTERCOOLER(S) TOTAL
22
AFTERCOOLER
23
OIL COOLER(S)
ONE CONSOLE FOR
COMP'RS
MULTI-POINT SUPPORT AND GROUTING WITH GROUT & VENT HOLES.
,
GROUP
,
DIV
NON-HAZARDOUS
COOLANT TO BE
BASIC SYS. REQ'MTS (NORM. COOLANT FLOW DATA)
13
CLOSED, PIPING BY MFR.
CONSOLE TO BE OF DECK PLATE TYPE CONSTRUCTION SUITABLE FOR
ELECTRICAL CLASSIFICATION : CLASS
12
OIL COOLER(S)
STEAM
% ETHYLENE GLYCOL
SITE
FORCED
THERMO
STAND
FLOW
PRESSURE
INLET TEMP
OUTLET TEMP
FLOW
COOL'G
SYPHON
PIPE
gpm
psig
°F
°F
IND'TR
24
25
TOTAL FLOW
26
SYS. PRESSURES:
27
COOLANT RESERVOIR:
DESIGN,
psig
SIZE,
HYDROTEST,
FT IN DIA X
psig
FT IN HT.
RELIEF VALVE(S), SETTING
CAPACITY
28
@ NORMAL OPERATING LEVEL
29
RESERVOIR MATERIAL
30
31
LEVEL GAUGE
PUMPS: (CENTRIFUGAL ONLY)
32
33
MAIN
34
AUXILIARY
LEVEL SWITCH
DRIVER
SPEED
gpm
psig
BHP
HP
r/min
GUARD(S) REQ.'D FOR COUP'G(S)
MANUAL
MAIN PUMP
MAIN PUMP
AUTO
38
COOLANT HEAT EXCHANGER:
INSPECTION & CLEAN-OUT OPENINGS
REQ'D
PUMP CASING MATERIAL (Ref 6.14.2.1.5):
39
DRAIN VALVE
PRESS.
36
AUX.PUMP CONTROL:
INTERNAL COATING, TYPE
RAT'D FL'W
35
37
SHELL & TUBE
COUPLING MECH.SEAL
REQ'D
REQ'D
AUX PUMP
AUX PUMP
GUARD TYPE OR CODE
ON-OFF-AUTO SEL. SWITCH:
BY PURCH.
WIRING TO TERMINAL BOX:
BY PURCH.
SINGLE
DUAL W/TRANSFER VALVE
BY MANUFACTURER
BY MANUFACTURER
TEMA C
40
TEMA R (API 660)
(DATA SHEETS ATTACHED)
41
AIR COOLED EXCHANGER W/AUTO TEMP CONTROL (API 661 DATA SHEETS ATTACHED)
42
W/BYPASS & TEM. CONTROL VALVE
43
SEE SEPARATE COOLER DATA SHEET FOR DETAILS; SPECIFY % GLYCOL ON BOTH SIDES
MANUAL
AUTO
LOUVERS FOR AIR EXCH.
OF SHELL & TUBE
44
45
psig
GALLONS
SYS. COMPONENT SUPP.
MANUFACTURER
MODEL
MANUFACTURER
46
MAIN PUMP
47
AUXILIARY PUMP
TRANSFER VALVE(S)
48
MECHANICAL SEALS
PUMP COUPLING(S)
49
ELECTRIC MOTORS
50
STEAM TURBINES
MODEL
TEMP CONTROL VALVE(S)
51
52
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
ITEM NO.
REVISION NO.
PAGE
DATE
13
OF
17
BY
1
PULSATION SUPPRESSION DEVICES FOR RECIPROCATING COMPRESSORS
2
THESE SHEETS TO BE FILLED OUT FOR EACH SERVICE AND/OR STAGE OF COMPRESSION
3 APPLICABLE TO:
PROPOSALS
PURCHASE
91
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
AS BUILT
4 FOR/USER
5 SITE/LOCATION
AMBIENT TEMPERATURE MIN/MAX
6 COMPRESSOR SERVICE
NUMBER OF COMPRESSORS
7 COMPRESSOR MFG.
MODEL/TYPE
/
°F
8 SUPPRESSOR MFG.
9 NOTE:
Ind.Data Comp.'d Purch.
By Compr/Supp.Mfg.w/Proposal
By Mfg(s) after order
By Mfg(s)/Purchaser as Applicable
GENERAL INFORMATION APPLICABLE TO ALL SUPPRESSORS
10
11 TOTAL NUMBER OF SERVICES AND/OR STAGES
12 TOTAL NUMBER OF COMPRESSOR CYL.
TOTAL NUMBER OF CRANKTHROWS
13
ASME CODE STAMP
14
OTHER APPLICABLE PRESSURE VESSEL SPEC. OR CODE
15
LUBE SERVICE
16
RADIOGRAPHY (X-RAY OF WELDS):
17
SHOP INSPECTION
18
STROKE
GOVERNMENTAL CODES OF
NON-LUBE SERV.
WITNESSED
NO OIL ALLOWED INTERNALLY
NONE
WITNESS HYDROTEST
SPOT
in.
r/min
CODE REGULATIONS APPLY
100%
DRY TYPE INTER.CORR.COATING
IMPACT TEST
YES
NO
SPECIAL WELDING REQUIREMENTS
OUTDOOR STORAGE OVER 6 MONTHS
SPECIAL PAINT SPEC
OBSERVED
19
CYLINDER, GAS, OPERATING, AND SUPPRESSOR DESIGN DATA
20
21
SERVICE
STAGE NO.
22
COMPRESSOR MANUFACTURER'S RATED CAPACITY
23
LINE SIDE OPERATING PRESSURE
INLET,
psia
DISCHARGE,
24
OPERATING TEMP. WITHIN SUPPRESSORS
INLET,
°F
DISCHARGE,
25
ALLOWABLE PRESSURE DROP THROUGH SUPPRESSORS
ǻP
26
LBS/HR
SCFM
psi
/
MMSCFD
%
INLET SUPPRESSOR
27
SUPRESSOR TAG NUMBER
28
COMBINATION INLET SUPP SEPARATOR/INTERNALS
29
NO. (QTY) OF INLET & DISCH. SUPP. PER STAGE
30
31
ǻP
psia
°F
psi
/
%
DISCHARGE SUPPRESSOR
NO
/
ALLOWABLE PEAK-PEAK PULSE @ LINE SIDE NOZZLE
psi
/
%
psi
/
%
ALLOWABLE PEAK-PEAK PULSE @ CYL FLANGE NOZZLE
psi
/
%
psi
/
%
YES
YES
/
NO
YES
NO
32
33
DESIGN FOR FULL VACUUM CAPABILITY
34
MIN. REQ'D WORKING PRESSURE & TEMPERATURE
35
NOTE:
NO
YES
NO
After design, the actual MAWP & temp are to be determined
36
based on the weakest component and stamped on the
37
vessel. The actual MAWP is to be shown on pg.14 line 12
38
YES
psig,
@
°F
psig,
@
°F
and on the U1A Forms.
39
INITIAL SIZING VOL. PER FORMULA OF 7.9.3.2
40
NOTE:
This is a Reference
FT³
FT³
FT³
FT³
41
42
AS BUILT VOLUME (FT³)
43
44
45
46
47
48
49
50
51
52
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
API STANDARD 618
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
Revision
92
ITEM NO.
REVISION NO.
PAGE
DATE
14
OF
17
BY
1
PULSATION SUPPRESSION DEVICES FOR RECIPROCATING COMPRESSORS (CONT'D)
SERVICE
2
THESE SHEETS TO BE FILLED OUT FOR EACH SERVICE AND/OR STAGE OF COMPRESSION
STAGE NO.
INLET SUPPRESSOR
3 CONSTRUCTION REQUIREMENTS & DATA
4
SUPRESSOR TAG NUMBER
5
BASIC MATERIAL REQUIRED, CS, SS, ETC.
6
ACTUAL MATERIAL DESIGNATION
SHELL/HEAD
7
SPECIAL HARDNESS LIMITATIONS, Rc
YES
8
CORROSION ALLOWANCE., in.
NO
WALL THICKNESS, in.
NOM. SHELL DIA X OVERALL LGTH.
11
PIPE OR ROLLED PLATE CONSTRUCTION
12
ACT. MAX ALLOW. WORKING PRESS. AND TEMPERATURE
13
MINIMUM DESIGN METAL TEMP (6.15.8.1)
14
INLET SUPRESS. TO BE SAME MAWP AS DISCH'RGE SUPPRESS.
15
MAX EXPECTED PRESSURE DROP( ' P, PSI / %) LINE PRESS
16
WEIGHT (lb EACH)
SHELL/HEAD
(in./vol. ft³)
x
19
20
SUPPORTS, TYPE/QUANTITY
22
LINE SIDE FLANGE.
23
COMP CYL FLANGE(S), QTY/SIZE/RATING/FACING/TYPE
24
FLANGE FINISH,
PER 7.9.5.1.16
>125 <250
26
INSPECTION OPENINGS REQUIRED
35
36
37
38
39
40
41
ROLLED PLATE
in.
ft³
in./
PIPE
°F
ROLLED PLATE
PSI @
°F
YES
'P
°F
NO
psi/
%
' P
psi/
%
%/
lb
%
%/
%
SIZE/RATING/FACING/TYPE
25
34
in./
x
CONNECTION REQUIREMENTS & DATA
21
33
ft³
lb
INSUL NUTS & ALLOW. FOR INSULATION REQUIRED (X)
32
WELDS
°F
EXPECTED P-P PULSE @ LINE SIDE/CYL FLG, % LINE PRESS
BASED ON FINAL SUPPRESSOR DESIGN
31
in.
in./
PSI @
17
30
SHELL & HEADS
in.
in./
PIPE
18
29
/
WELDS
in.
9
28
/
SHELL & HEADS
REQUIRED
10
27
DISCHARGE SUPPRESSOR
SPECIAL (SPECIFY)
PER ANSI 16.5
YES
NO
BLINDED
YES
NO
BLINDED
SPEC. QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
* QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
VENT CONNECTIONS REQUIRED
YES
NO
YES
NO
YES
NO
YES
NO
YES
NO
YES
NO
YES
NO
YES
NO
SPEC. QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
* QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
DRAIN CONNECTIONS REQUIRED
SPEC. QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
* QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
PRESSURE CONNECTIONS REQUIRED
SPEC. QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
* QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
TEMPERATURE CONNECTIONS REQUIRED
SPEC. QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
CYL NOZZLE
MAIN BODY
* QTY. SIZE, 6000 LB NPT CPLG./FLG TYPE & RATING
42
43
44
45
OTHER DATA AND NOTES
46
47
COMPRESSOR MFG'S SUPP. OUTLINE OR DRAWING NO.
48
SUPP. MFG'S OUTLINE OR DRAWING NO.
49
NOTES * = AS BUILT
50
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
JOB NO.
ITEM NO.
REVISION NO.
DATE
PAGE
15
OF
17
93
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
BY
INSTRUMENTATION
1
2 PURCHASER TO FILL IN
(
) AFTER COMMODITY TO INDICATE:
3
INSTRUMENT & CONTROL
ONE FOR EA. UNIT
4
PANEL
MACHINE MT'ED
(
):
BY COMP. MFR.
BY PURCH.
BY OTHERS
REMOTE
OUTDOORS
ONE COMMON TO ALL UNITS
FREE STANDING (OFF UNIT)
ELEC.
ELECTRONIC
LOCAL
5
PNEUMATIC
HYDRAULIC
6
NEMA 7, CLASS
, GROUP
7
I/S BARRIERS (
)
8
NEMA 4, WATERTIGHT & DUSTTIGHT
9
OTHER NEMA
10
VIB, ISOLATORS
11
ANNUNCIATOR W/FIRST-OUT INDICATION LOCATED ON CONTROL PANEL
, DIVISION
PROGRAMMABLE CONTL'R
INTRINSICALLY SAFE
PURGED TO NFPA 496 TYPE
LOW PURGE PRESS.
STRIP HEATERS
X
ALARM
PURGE CONN.
Y
Z
SHUTDOWN
EXTRA CUTOUTS
PURCHASER'S CONN. BROUGHT OUT TO TERMINAL BOX BY VENDOR
12
13
BUFFER GAS CONTROL
14
PANEL
(
):
ONE FOR EA. UNIT
ONE COMMON TO ALL UNITS
MACHINE MT'ED
FREE STANDING (OFF UNIT)
15
CLASS
, GROUP
16
CONSTANT PRESSURE DISPOSAL SYSTEM
WITH STAND
OUTDOORS
, DIVISION
VARIABLE PRESSURE DISPOSAL SYSTEM
17 ADDITIONAL PANEL REMARKS:
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
18
19
20
INSTRUMENTATION SUITABLE FOR:
INDOORS
OUTDOORS
OTHER
21
PREFERRED INSTRUMENT SUPPLIERS, (TO BE COMPLETED BY PURCHASER), OTHERWISE MFR'S STANDARD APPLIES
22
PRESSURE GAUGES
MFR
SIZE & TYPE
MTL
23
TEMPERATURE GAUGES
MFR
SIZE & TYPE
MTL
24
LIQUID LEVEL GAUGES
MFR
25
DIFF. PRESSURE GAUGES
MFR
26
PRESS. TRANSMITTERS
MFR
TYPE
27
LIQUID LEV. TRANSMITTER
MFR
TYPE
MTL
28
PRESSURE SWITCHES
MFR
TYPE
MTL
29
TEMPERATURE SWITCHES
MFR
TYPE
MTL
30
LIQUID LEVEL SWITCHES
MFR
TYPE
MTL
31
DIFF. PRESSURE SWITCHES
MFR
TYPE
MTL
32
CONTROL VALVES
MFR
TYPE
MTL
33
PRESSURE SAFETY VALVES
MFR
TYPE
MTL
34
SIGHT FLOW INDICATORS
MFR
TYPE
MTL
35
VIBRATION MONITORS & EQUIP.
MFR
TYPE
MTL
36
THERMOCOUPLES
MFR
TYPE
MTL
37
RTD'S
MFR
TYPE
MTL
38
SOLENOID VALVES
MFR
TYPE
MTL
39
ANNUNCIATOR
MFR
40
PROGRAMMABLE CONTROLLER
MFR
41
42
TYPE
MTL
MTL
(
MODEL & (QTY SPARE POINTS)
TYPE
MFR
PRESSURE GAUGE REQUIREMENTS
MTL
SIZE & TYPE
TYPE
LIQUID-FILLED PRESSURE GAUGES:
)
MTL
MTL
YES
NO
43
LOCALLY
PANEL
LOCALLY
PANEL
44 FUNCTION
MOUNTED
MOUNTED
MOUNTED
MOUNTED
45
LUBE OIL MAIN PUMP DISCHAR.
(
)
(
)
PROCESS GAS: INLET PRESS.
(
)
(
)
46
LUBE OIL AUX. PUMP DISCHARG.
(
)
(
)
@ EA. STAGE
(
)
(
)
47
LUBE OIL PRESS. AT FRAME HEADER (
)
(
)
DISCH. PRESS.
(
)
(
)
48
LUBE OIL FILTER ǻP
(
)
(
)
@ EA. STAGE
(
)
(
)
49
COOLING H2O INLET HEADER
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
50
51 REMARKS:
52
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
API STANDARD 618
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
ITEM NO.
REVISION NO.
PAGE
DATE
16
OF
17
BY
INSTRUMENTATION (CONT'D)
1
2 TEMPERATURE MEASUREMENT REQUIREMENTS
LOCALLY
PANEL
3 FUNCTION
MOUNTED
MOUNTED
4
LUBE OIL
INLET TO
OUT OF
FRAME
(
)
(
)
LUBE OIL
INLET TO
OUT OF
COOLER
(
)
(
)
6
MAIN JRNL BEARINGS (THERMOCOUPLES OR RTD'S ONLY)
(
)
(
)
7
MOTOR BEARING(S)
(
)
(
)
(THERMOCOUPLES OR RTD'S ONLY)
8
CYL. COOLANT MANIFOLD:
9
CYL. JKT. COOLANT:
INLET
INLET
OUTLET
OUTLET
EA. CYL
(
)
(
)
(
)
(
)
10
PROCESS GAS:
INLET
DISCH.
EACH CYL
(
)
(
)
11
INTERCOOLER(S)
INLET
GAS
COOLANT
(
)
(
)
OUTLET
GAS
COOLANT
(
)
(
)
AFTERCOOLER:
INLET
GAS
COOLANT
(
)
(
)
OUTLET
GAS
COOLANT
PKG COOLANT
INLET
OUTLET
12
14
15
(
)
(
)
(
)
(
)
16
PRESS. PGK CASE, CYL PIST ROD (THRM'CPLS OR RTD'S ONLY)
(
)
(
)
17
COMPRESSOR VALVES
(
)
(
)
18
(
)
(
)
19
(
)
(
)
20
SUCT.
DISCH. TC'S OR RTD'S ONLY
I/S
SYS
SYS
ANNUNCIATION POINTS
22
ALARM DEVICES:
TRANSMITTER
SWITCH
23
SHUTDOWN DEVICES
TRANSMITTER
SWITCH
ALARM
25
ALARM
FUNCTION
IN CTL
IN
IN CTL
TOTAL
PNL
ROOM
PNL
ROOM
NO.
SHUT
BY
PANEL
BY
PANEL
OF
DOWN
MFR
OTH'RS
MFR
OTH'RS
POINTS
27
LOW LUBE OIL PRESS. @ BEARING HEADER
(
) (
)
28
HIGH LUBE OIL ǻP AP ACROSS FILTER
(
) (
)
29
LOW LUBE OIL LEVEL, FRAME
(
) (
)
30
AUX LUBE OIL PUMP, FAIL TO START
(
) (
)
31
CYL LUBE SYSTEM PROTECTION
(
) (
)
32
COMPR. VIBRATION, SHUTDOWN ONLY
33
VIBRATION, W/ CONTINUOUS MONITORING
34
35
(
)
(
) (
)
ROD DROP DETECTOR, CONTACT TYPE(1/CYL)
(
) (
)
ROD DROP PROXIMITY PROBE (1/CYL)
(
) (
)
36
OIL TEMP OUT OF FRAME
(
) (
)
37
HIGH GAS DISCH. TEMP EACH CYLINDER
(
) (
)
38
HIGH JACKET COOLANT TEMP., EA. CYL
(
) (
)
39
LOW SUCTION PRESS., FIRST STG INLET
(
) (
)
40
HI DISCH. PRESS.
(
) (
)
41
HI CYL. GAS ' P, EACH STAGE
(
) (
)
42
HI LIQ. LEV., EA. MOISTURE SEPARATOR
(
) (
)
43
LOW PURGE GAS PRESS, DISTANCE PIECE(S)
(
) (
)
44
HI X-HD PIN TEMP
(
) (
)
45
PRESS PKG CASE (PISTON ROD TEMP)
(
) (
)
(
) (
FINAL
46
EA STG
47
SHUTDOWN
IN
24
)
TOTAL NUMBER OF ANNUNCIATION POINTS
48
SWITCH CONTACT OPERATION
49
ALARM CONTACTS SHALL:
50
51
RTD
NOTE: ALARM & SHUTDOWN DEVICES SHALL BE INDIVIDUALLY SEPARATE
ALARM & SHUTDOWN SYSTEM REQ'MTS
21
26
THERMO
CAPILLARY CPL SYS
GAUGE W/
5
13
Revision
94
NOTE: EACH SWITCH SHALL BE MINIMUM SPDT ARRANGEMENT
OPEN ( DE-ENER.) TO SOUND ALARM & BE ENERGIZED WHEN COMPR. IS IN OPERATION
CLOSE (ENERGIZE) TO SOUND ALARM & BE DE-ENERGIZED WHEN COMPR. IS IN OPERATION
SHUTDOWN CONTACTS SHALL:
52
OPEN ( DE-ENERGIZED) TO SHUTDOWN & BE ENERGIZE WHEN COMPR. IS IN OPERATION
CLOSE (ENERGIZE) TO SHUTDOWN & BE DE-ENERGIZE WHEN COMPR. IS IN OPERATION
53 REF: 7.6.6.2 FOR MINIMUM RECOMMENDED PROTECTION REQUIREMENTS
S 618 16
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
U.S. CUSTOMARY UNITS
3
ITEM NO.
REVISION NO.
DATE
PAGE
SIGHT FLOW IND. (COOLANT ONLY)
(
)
FOR:
PNEUMATIC PRESSURE TRANSMITTERS
(
)
FOR:
6
PRESSURE TRANSMITTERS (ELEC. OUTP.)
(
)
FOR:
7
PNEUMATIC LEVEL TRANSMITTERS
(
)
8
ALARM HORN & ACKN'LMT TEST BUTTON
(
)
9
CONDUIT & WIRING W/JUNCT. BOXES
(
)
10
TEST VALVES
(
)
FOR:
11
DRAIN VALVES
(
)
FOR:
12
GAUGE GLASS(ES)
(
)
FOR:
13
TACHOMETER
(
)
14
CRANKSHAFT KEY PHASER
(
)
15
AND TRANSDUCER
(CONSOLES)
(
16
INTERCOOLER(S)
AFTER CLR
OIL COOLER
ROD PRESS. PKG COOLANT
SPEED RANGE
TO
(
)
(
)
20
(
)
21
(
)
22
(
)
23
(
SEPARATE COOLING WATER CONSOLE INSTRUMENT:
)
PURCH. TO LIST REQ'MTS IN ADDITION TO ANY ABOVE REQ'MTS
25
(
)
26
(
)
27
(
)
28
(
)
29
(
)
30
(
)
RELIEF VALVES
LOCATION
32
BY
MANUFACTURER
33
(
)
34
(
)
35
(
)
36
(
)
37
(
)
38
(
)
39
(
)
40
(
)
41
(
)
42
(
)
NOTES:
TYPE
SIZE
FOR TURBINE DRIVERS USE APPLICABLE API DATA SHEETS
45
FOR GEAR REDUCERS USE APPLICABLE API DATA SHEETS
46
ELECTRICAL & INSTRUMENTATION CONNECTIONS SHALL BE MADE DIRECTLY BY THE PURCHASER TO INDIVIDUAL
48
SETTING
SEE MOTOR DATA SHEET FOR ADDITIONAL MOTOR INSTRUMENTATION REQUIREMENTS
44
47
r/min
FOR:
)
19
43
BY
PURCH. TO LIST REQ'MTS IN ADDITION TO ANY ABOVE REQ'MTS
SEPARATE LUBE OIL CONSOLE INSTRUMENTATION:
18
31
17
CYL JACKET COOLANT
5
24
OF
MISCELLANEOUS INSTRUMENTATION
4
17
17
INSTRUMENTATION (CONT'D)
1
2
JOB NO.
95
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
INSTRUMENTS ON THE COMPRESSOR
ADDITIONAL INSTRUMENTATION REMARKS/SPECIAL REQUIREMENTS:
49
50
51
Figure A-1—Reciprocating Compressor Data Sheet (U.S. Customary Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
API STANDARD 618
JOB NO.
ITEM NO.
Revision
96
PURCHASE ORDER NO.
SPECIFICATION NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
1 APPLICABLE TO:
PROPOSALS
2 FOR/USER
3 NOTE:
PURCHASE
DATE
1
OF
BY
SERVICE
NO. WITH CYLS.
NO. REQ'D
BY MANUFACTURER
AFTER ORDER
TYPE MODEL NO(S)
6 COMPR.THROWS: TOTAL NO.
17
AS BUILT
BY MANUFACTURER
WITH PROPOSAL
5 COMPR. MFGR
7
PAGE
SITE/LOCATION
INDICATES INFO. TO BE
COMPLETED BY PURCH.
4
REVISION NO.
BY MANUFACTURER OR
PURCHASER AS APPLICABLE
SERIAL NO(S)
NOMINAL FRAME RATING
MAX/MIN ALLOWABLE SPEED
/
8 DRIVER MFGR.
BkW @ RATED R/MIN OF
r/min
DRIVER NAMEPLATE HP/OPERATING r/min
9 DRIVE SYSTEM:
DIRECT COUPLED
GEARED & COUPLED
10 TYPE OF DRIVER:
IND. MOTOR
11
CYLINDERS CONSTRUCTION:
SYN. MOTOR
/
V-BELT
STEAM TURBINE
GAS TURBINE
LUBE
NON-LUBE
ENGINE
OTHER
12
13
MAX ACCEPTABLE AVG PISTON SPEED
m/s
OPERATING CONDITIONS (EACH MACHINE)
14
15
SERVICE OR ITEM NO.
16
STAGE
17
NORM. OR ALT. CONDITION
18
CERTIFIED PT. (X) MARK ONE
19
MOLECULAR WEIGHT
20
CP/CV (K) @ 65°C OR
°C
21
INLET CONDITIONS:
AT INLET TO:
22
NOTE:
23
PRESSURE (bar) @ PUL. SUPP. INLET
24
PRESSURE (bar) @ CYL. FLANGE
25
TEMPERATURE (°C)
26
REC: SIDE STREAM TEMPS (°C)
27
COMPRESSIBILITY (Zs )
28
INTERSTAGE:
29
ǻP BETWEEN STAGES, %/bar
INTERSTAGE ' P INCL:
30
DISCHARGE CONDITIONS:
31
PRESSURE (bar) @ CYL. FLANGE
32
PRESS. (bar) @ PUL. SUPP. OUTLET
33
TEMP., ADIABATIC, °C
34
TEMP., PREDICTED, °C
35
COMPRESSIBILITY (Z2 ) OR (ZAVG )
PULSE DEVICES
COMPRESSOR CYLINDER FLANGES
SIDE STREAM TO
STAGE(S), THESE INLET PRESS. ARE FIXED
PULSE DEVICES
AT OUTLET FROM:
PULSE DEVICE
PIPING
COOLERS
COMP. CYL. FLANGES
SEPARATORS
OTHER
36 * CAPACITY AT INLET TO COMPRESSOR, NO NEGATIVE TOLERANCE (-0%)
37
CAPACITY SPECIFIED
kg/h
38
IS
WET
DRY
m3/h (1 bar & 60°C)
39
40 * MFGR.'S RATED CAPACITY (AT INLET TO COMPRESSSOR & kW @ CERTIFIED TOLERANCE OF ±3% FOR CAP. & ±3% FOR kW)
41
43
44
45
46
47
48
49
50
51
CAPACITY SPECIFIED
kg/h
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
42
IS
WET
DRY
3
INLET VOLUME FLOW (m /h)
MMSCCD/SCCM (14.7 PSIA & 60°C)
BkW/STAGE
TOTAL BkW @ COMPRESSOR SHAFT
TOTAL kW INCLUDING
V-BELT & GEAR LOSSES
* CAPACITY FOR NNT
REMARKS:
MANUFACTURER'S = REQUIRED ÷ 0.97
THEREFORE REQUIRED = MFR'S x 0.97
Figure A-2—Reciprocating Compressor Data Sheet (SI Units)
OTHER
1
ITEM NO.
REVISION
DATE
PAGE
2
OF
17
BY
GAS ANALYSIS AT OPERATING CONDITIONS
MOLE % (BY VOLUME) ONLY
2
3
SERVICE/ITEM NO.
4
STAGE
5
NORMAL OR ALT
6
REMARKS
M.W.
7 AIR
28.966
8 OXYGEN
O2
9 NITROGEN
N2
28.016
10 WATER VAPOR
H2O
18.016
11 CARBON MONOX.
CO
28.010
12 CARBON DIOX.
CO2
44.010
13 HYDRO. SULFIDE
H2S
34.076
32.000
14 HYDROGEN
H2
2.016
15 METHANE
CH4
16.042
16 ETHYLENE
C2H4
28.052
17 ETHANE
C2H6
30.068
18 PROPYLENE
C3H6
42.078
19 PROPANE
C3H8
44.094
20 I-BUTANE
C4H10
58.120
21 n-BUTANE
C4H10
58.120
22 I-PENTANE
C5H12
72.146
23 n-PENTANE
C5H12
72.146
25 AMMONIA
NH3
17.031
INDUSTRY SERVICES
26 HYDRO. CHLOR.
HCI
36.461
NACE MR-O175 (6.15.1.11)
27 CHLORINE
Cl2
70.914
APPLICABLE SPECIFICATIONS
API 618, RECIPROCATING COMPRESSORS
FOR PETROLEUM, CHEMICAL AND GAS
24 HEXANE PLUS
28 CHLORIDES - TRACES
29
30
31
32
33
CALCULATED MOL WT.
Cp/Cv (K) @ 65° OR
°C
34 NOTE:
IF WATER VAPOR AND/OR CHLORIDES ARE PRESENT, EVEN MINUTE
35
TRACES, IN THE GAS BEING COMPRESSED, IT MUST BE INCLUDED ABOVE.
36
37 ELEVATION
SITE/LOCATION CONDITIONS
m
bar
AMBIENT TEMPS: MAX
38
MIN DESIGN METAL TEMP
°C (6.15.8.1)
39 COMPRESSOR LOCATION:
INDOOR
HEATED
UNHEATED
40
OUTDOOR
NO ROOF
UNDER ROOF
41
OFF-SHORE
42
WINTERIZATION REQUIRED
43 UNUSUAL CONDITIONS:
CORROSIVES
°C MIN
AT GRADE LEVEL
PARTIAL SIDES
WEATHER PROTECTION REQ.
DUST
FUMES
°C
RELATIVE HUMIDITY: MAX
%
MIN
%
ELEVATED:
PLATFORM:
m
ON-SHORE
TROPICALIZATION REQ.
OTHER
44
45
ELECTRICAL CLASSIFICATIONS
46
HAZARDOUS
NON-HAZARDOUS
47 MAIN UNIT
CLASS
GROUP
DIVISION
48 L.O. CONSOLE
CLASS
GROUP
DIVISION
49 CW CONSOLE
CLASS
GROUP
DIVISION
50
51
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
97
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
1
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
3
OF
17
Revision
98
BY
PART LOAD OPERATING CONDITIONS
2 CAPACITY CONTROL
BY:
3
FOR:
4
WITH:
5
USING:
MFG'S CAP. CONTROL
PURCHASERS BY-PASS
BOTH
PART LOAD COND.
START-UP ONLY
BOTH
AUTO LOADING DELAY INTERLOCK (7.6.2.4)
FIXED VOLUME POCK.
AUTO IMMEDIATE UNLOADING
SUCTION VALVE UNLOADERS:
6
ACTION:
7
NUMBER OF STEPS:
OTHER
FINGER
PLUG
DIRECT (AIR-TO-UNLOAD)
ONE
OTHER
REVERSE (AIR-TO-LOAD/FAIL SAFE)
THREE
FIVE
OTHER
RAIN COVER REQUIRED OVER UNLOADERS
8
9
ALL UNLOADING STEPS BASIS MANUFACTURERS CAPACITY SHOWN ON PAGE 1.
10 INLET AND DISCHARGE PRESSURE ARE
AT CYLINDER FLANGES
11
SERVICE OR ITEM NO.
12
STAGE
13
NORMAL OR ALTERNATE CONDITION
14
PERCENT CAPACITY
15
WEIGHT FLOW, kg/h
16
MMSCFD/SCFM (14.7 bar & 60°C)
17
POCKETS/VALVES OPERATION *
18
POCKET CLEARANCE ADDED %
19
TYPE UNLOADERS, PLUG/FINGER
20
INLET TEMPERATURE, °C
21
INLET PRESSURE, bar
22
DISCHARGE PRESSURE, bar
23
DISCHARGE TEMP., ADIABATIC °C
24
DISCHARGE TEMP., PREDICTED °C
25
VOLUMETRIC EFF.,%HE/%CE
26
CALC. GAS ROD LOAD, kN, C **
27
CALC. GAS ROD LOAD, kN, T **
28
COMB. ROD LOAD, LB C (GAS & INERTIA)
29
COMB. ROD LOAD, LB T (GAS & INERTIA)
30
ROD REV., DEGREES MIN @ X-HD PIN ***
31
kW/STAGE
32
TOTAL kW @ COMPRESSOR SHAFT
33
TOTAL kW INCL. V-BELT & GEAR LOSSES
PULSATION SUPPRESSOR FLANGES
34
35
* SHOW OPERATION WITH THE FOLLOWING SYMBOLS:
36
37
HEAD END
38
OR
39
CRANK END
=
HE
=
CE
½
¾
¿
PLUS
40
­
°
®
°
¯
SUCTION VALVE(S) UNLOADED
=
S
=
F
=
V
OR
FIXED POCKET OPEN
OR
VARIABLE POCKET OPEN
41
42
EXAMPLE:
HE-F/CE-S = HEAD END FIXED POCKET OPEN / CRANK END SUCTION VALVE(S) UNLOADED.
43
* * C = COMPRESSION
44
MINIMUM PRESSURE REQUIRED TO OPERATE CYLINDER UNLOADING DEVICES,
45 CYLINDER UNLOADING MEDIUM:
46
T = TENSION
AIR
*** X - HD = CROSSHEAD
NITROGEN
PRESSURE AVAILABLE FOR CYLINDER UNLOADING DEVICES, MAX/MIN
barg
OTHER
/
barg
47 REMARKS, SPECIAL REQUIREMENTS, AND/OR SKETCH
48
49
50
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,
51
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
4
OF
17
BY
SCOPE OF BASIC SUPPLY
1
2
PURCHASER TO FILL IN
3
DRIVER
(
(
) AFTER COMMODITY TO INDICATE:
):
VARIABLE SPEED
BY COMPR. MFR.
SPEED RANGE
BY PURCH.
r/min TO
INDUCTION MOTOR
SYNCHRONOUS MOTOR
STEAM TURBINE
ENGINE
5
API 541
API 546
API 611
API 612
6
OUTBOARD BEARING
7
SLIDE BASE FOR DRIVER (
8
MOTOR STARTING EQUIPMENT
9
GEAR (
10
COUPLING(S) (
11
):
)
(
)
); DEFINE
BASEPLATE FOR GEAR
):
OTHER
PROVISION FOR DRY AIR PURGE FOR OUTBOARD BEARING.
SOLE PLATE FOR DRIVER
(
BY OTHERS
r/min
4
LOW SPD.
API 613
HI-SPD.
API 677
QUILL SHAFT
KEY-LESS DRV.
KEY'D DRV.
OTHER
API 671
12
V-BELT DRIVE (
13
DRIVE GUARD(S) (
):
SHEAVES & V-BELTS (
):
)
MANUFACTURER'S STD.
14
15
99
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
STATIC CONDUCTING V-BELTS
NON-SPARKING
CALIF CODE
BANDED V-BELTS
API 671, ANNEX G
OTHER
PULSATION SUPPRESSORS
(
):
16
INITIAL INLET & FINAL DISCHARGE
SUPPORTS
(
)
INTERSTAGE
SUPPORTS
(
)
ALL INTERSTAGE INLET
17
SUPPRESSOR(S) TO HAVE MOISTURE REMOVAL SECTION:
INITIAL INLET
18
ACOUSTICAL SIMUL. STUDY
DESIGN
1,
EMPIRICAL PULSATION SUPRESSION DEVICE SIZING
19
APPROACH
2,
ACOUSTIC SIMULATION AND PIPING RESTRAINT ANALYSIS
20
CHECK ONLY ONE, SEE 7.9.4.1.1, TABLE 6)
3,
ACOUSTIC SIMULATION AND PIPING RESTRAINT ANALYSIS
(
):
PLUS MECHANICAL ANALYSIS
21 STUDY TO CONSIDER:
22
ALL SPECIFIED LOAD COND., INCL.
SINGLE ACT., PLUS
COMP.OPER.IN PARALLEL
ALTERNATE GASES
23
CRITICAL FLOW MEASUREMENT (7.9.4.2.5.3.3)
WITH EXISTING COMP. AND PIPING SYSTEMS
24
PULSATION SUPRESS'N DEVICE LOW CYCLE FATIGUE ANALYSIS
PIPING SYSTEM FLEXIBILITY
25
VENDOR REVIEW OF PURCHASER'S PIPING ARRANGEMENT
26 NOTE: SEE APPENDIX N FOR INFORMATION REQUIRED FOR STUDY
27
PACKAGED:
28
DIRECT GROUTED
29
RAILS
30
NO
YES
(
)
DEFINE BASIC SCOPE OF PACKAGING IN REMARKS SECTION, PAGE 5
CEMENTED/MORTAR GROUT
CHOCK BLOCKS
SHIMS
EPOXY GROUT; MFG/TYPE
BASEPLT.
SKID
SOLEPLT.
/
BOLTS OR STUDS FOR SOLEPLT. TO FRAME
SUITABLE FOR COLUMN MOUNTING (UNDER SKID AND/OR BASEPLATE)
31
LEVELING SCREWS
32
INTERCLR(S) (
33
SEPARATOR(S)
NON-SKID DECKING
)
(
SUB SOLEPLATES
OFF MOUNTED
MACHINE MTD.
AFTERCLR(S) (
)
)
CONDENSATE SEPARATION & COLLECTION FACILITY SYSTEM (7.8.2.1)
):
FINAL DISC. PIP. (
34
INTERSTAGE PIP. (
35
FLANGE FINISH
):
36
SPECIAL PIPING REQUIREMENTS (7.7.1.13). (DEFINE IN REMARKS SECTION NEXT PAGE)
37
INITIAL INLET,
38
INLET STRAINER(S)
39
MANIFOLD PIPING;
40
RELIEF VALVE(S) (
):
INITIAL INLET
41
RUPTURE DISC(S) (
)
THRU STUDS IN PIPING FLANGES
42
FOR ATMOSPHERIC INLET AIR COMPR. ONLY:
43
PREFERRED TYPE OF CYLINDER COOLING
API 618 FLANGE FINISH > 125 < 250 (7.9.5.1.16)
INTERSTAGE SUCTION PIPING ARR'D FOR:
(
):
INITIAL INLET
DRAINS
VENTS
INSULATION
(
)
SIDESTREAM INLET
RELIEF VALVES
AIR/GAS SUPPLY
FINAL DISCHARGE
):
(
FORCED
HEAT TRACING
)
INLET FILTER -SILENCER
THERMOSYPHON
(
(
MANUFACTURER SHALL RECOMMEND
STATIC (STAND-PIPE)
45
BEST TYPE OF COOLING AFTER
CYL. COOLANT PIPING BY (
46
FINAL ENGINEERING REVIEW OF ALL
SINGLE INLET/OUTLET MANIFOLD & VALVES
47
OPERATING CONDITIONS
INDIVIDUAL INLET/ OUTLET PER CYL.
STAGE CYL'(S)
)
MATCH M'RKED
SIGHT GL'SS(ES)
VALVE(S)
CLOSED SYSTEM WITH PUMP, COOLER, SURGE TANK, & PIPING
49
50
51
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
)
STAGE CYL'(S)
44 NOTE:
48
SHOP FITTED
SPECIAL FINISH
SPOOL PIECE FOR INLET STRAINERS
INTERSTAGE
INLET AIR FILTER
(
PARTIAL PRE FAB, FIELD FIT
FLANGE FINISH PER ANSI 16.5
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
SEPARATE COOLING CONSOLE (
):
DATE
PAGE
5
OF
17
BY
ONE FOR EA. UNIT
ONE CMMN TO ALL UNITS
DUAL PUMPS (AUX .& MAIN)
ARRANGED FOR HEATING JACKET WATER AS WELL AS COOLING
3
4
ROD PRESS. PACKING COOLING SYSTEM
5
FRAME LUBE OIL SYSTEM (
(
):
):
SEPARATE CONSOLE
AUX. PUMP
SHOP RUN
COMBINE WITH JKT SYSTEM
DUAL FILTERS WITH TRANSFER VALVE
FILTERS
SHOP RUN
CONTINUOUS FLOW IN SENSING LINE TO PRESSURE SWITCHES
6
7
ITEM NO.
REVISION
SCOPE OF BASIC SUPPLY (Con't)
1
2
JOB NO.
Revision
100
SEPARATE LUBE OIL CONSOLE (
):
EXTENDED TO MOTOR OUTBOARD BEARING
SHOP RUN
NOTE: PIPING BETWEEN ALL CONSOLES AND COMPRESSOR UNIT BY PURCHASER
8
SEE DATA SHEET PAGE 3 FOR DETAILS
IN INSTRUMENT & CONTROL PANEL
10
SEPARATE MACHINE MOUNTED PANEL
SEPARATE FREE STANDING PANEL
11
PNEUMATIC
HYDRAULIC
12
PROGRAMMABLE CONTROLLER
9
13
CAPACITY CONTROL (
):
INSTRUMENT & CONTROL PANEL (
ELECTRIC
):
ONE FOR EACH UNIT
14
15
BUFFER GAS CONTROL PANEL (
):
16
17
18
19
ELECTRONIC
ONE COMMON TO ALL UNITS
MACHINE MOUNTED
FREE STANDING (OFF UNIT)
ONE FOR EACH UNIT
ONE COMMON TO ALL UNITS
MACHINE MOUNTED
FREE STANDING (OFF UNIT)
SEE INSTRUMENTATION DATA SHEETS FOR DETAILS OF PANEL, ADDITIONAL REMARKS, AND INSTRUMENTATION.
NOTE:
ALL TUBING, WIRING, & CONNECTIONS BETWEEN OFF-UNIT FREE STANDING PANELS AND COMPRESSOR UNIT BY
PURCHASER.
20
21
HEATERS (
):
22
FRAME LUBE OIL
CYL. LUBRICATORS
ELECTRIC
STEAM
COOLING WATER
DRIVER(S)
GEAR OIL
23
BARRING DEVICE
CRANKCASE RAPID PRESSURE RELIEF DEVICE(S) (
(
):
MANUAL
26
SPECIAL CORROSION PROTECTION:
27
HYDRAULIC TENSIONING TOOLS
28
MECHANICAL RUN TEST:
NO
NO
NO
PNEUMATIC
ELECTRIC
FLYWHEEL LOCKING DEVICE
YES
MFR'S STANDARD
OTHER
YES
YES
MFG'S STANDARD
OTHER
COMPLETE SHOP RUN TEST OF ALL MACHINE MOUNTED EQUIPMENT, PIPING & APPURT.'(S)
29
30
31
PAINTING:
MANUFACTURER'S STANDARD
32
NAMEPLATES:
U.S. CUSTOMARY UNITS
33
SHIPMENT:
DOMESTIC
EXPORT
SPECIAL
SI UNITS
EXPORT BOXING REQUIRED
STANDARD 6 MONTH STORAGE PREPARATION
34
OUTDOOR STORAGE FOR OVER 6 MONTHS (
35
(
(
)
), PER SPEC
), PER SPEC
36
INITIAL INSTALLATION AND OPERATING TEMP ALIGNMENT CHECK AT JOBSITE BY VENDOR REPRESENTATIVE
37
COMPRESSOR MANUFACTURER'S USER'S LIST FOR SIMILAR SERVICE
38
COMPRESSOR VALVE DYNAMIC RESPONSE
39
PERFORMANCE DATA REQUIRED (9.3.3):
BHP VS. SUCTION PRESSURE CURVES
40
ROD LOAD/GAS LOAD CHARTS
41
VALVE FAILURE DATA CHARTED
SPEED/TORQUE CURVE DATA
42
43
BkW VS. CAPACITY PERFORMANCE CURVES OR TABLES REQUIRED FOR UNLOADING STEPS AND/OR VARIABLE
44
SUCTION/DISCHARGE PRESSURES
45
46
(
)
)
REMARKS:
47
48
49
50
51
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
24
25
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
6
OF
17
101
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
BY
UTILITY CONDITIONS
1
2 ELECTRICAL POWER:
AC VOLTS /
PHASE
/
HERTZ
DC VOLTS
AC VOLTS
3
MAIN DRIVER
/
/
INSTRUMENT
4
AUXILIARY MOTORS
/
/
ALARM & SHTDWN
5
HEATERS
/
/
/
PHASE
/
/
HERTZ
/
DC VOLTS
/
/
/
/
/
/
/
6
7
8 INSTRUMENT AIR:
NORMAL PRESSURE
barg
MAX/MIN
/
9 NITROGEN:
NORMAL PRESSURE
barg
MAX/MIN
/
FOR:
10 STEAM
DRIVERS
barg
MAX/MIN
/
12 (NORM.)
°C
MAX/MIN
/
13 EXH'ST: PRESS
barg
MAX/MIN
/
14 (NORM.)
°C
MAX/MIN
/
FOR:
COMPRESSOR CYLINDERS
TEMP
barg
HEATERS
11 INLET: PRESS
TEMP
barg
barg INLET: PRESS
°C
(NORM.) TEMP
barg EXH'ST:PRESS
°C
(NORM.) TEMP
barg
MAX/MIN
/
°C
MAX/MIN
/
barg
°C
barg
MAX/MIN
/
barg
°C
MAX/MIN
/
°C
barg
15
16
17 COOLING WATER
18
TYPE WATER
19 SUPP.: PRESS
barg
MAX/MIN
/
20 (NORM.)
°C
MAX/MIN
/
barg
MAX/MIN
/
°C
MAX/MIN
/
21 R'T'RN:
COOLERS
TYPE WATER
TEMP
PRESS
22 (NORM.)
TEMP
barg SUPP.: PRESS
°C
(NORM.) TEMP
barg R'T'RN: PRESS
°C
(NORM.) TEMP
barg
MAX/MIN
/
°C
MAX/MIN
/
°C
barg
MAX/MIN
/
barg
°C
MAX/MIN
/
°C
23
24 COOLING FOR ROD PACKING:
25 TYPE FLUID
SUPPLY PRESSURE
26 FUEL GAS:
NORMAL PRESSURE
27
COMPOSITION
barg @
barg
MAX/MIN
°C
RETURN
/
barg
barg @
LHV
°C
3
MJ/m
28
29 REMARKS/SPECIAL REQUIREMENTS:
30
31
32
33
34
35
36
37
38
39
40
41
42
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
43
44
45
46
47
48
49
50
51
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
7
OF
17
Revision
102
BY
CYLINDER DATA AT FULL LOAD CONDITION
1
2 SERVICE/ITEM NO.
3 STAGE
}
4 INLET PRESSURE, barg
5 DISCHARGE PRESSURE, barg
@ CYLINDER
FLANGES
6 CYLINDERS PER STAGE
7 SINGLE OR DOUBLE ACTING (SA OR DA)
8 BORE, mm
9 STROKE, mm
10 RPM:
RATED / MAX ALLOW
11 PISTON SPEED, m/s:
RATED / MAX ALLOW
12 CYLINDER LINER, YES/NO
13 LINER NOMINAL THICKNESS, mm
3
14 PISTON DISPLACEMENT, m /h
15 CYLINDER DESIGN CLEARANCE, % AVERAGE
16 VOLUMETRIC EFFICIENCY, % AVERAGE
17 VALVES, INLET/DISCHARGE, QTY PER CYL.
18 TYPE OF VALVES
19 VALVE LIFT, INLET/DISCHARGE, mm
20 VALVE VELOCITY, m/s
21
SUCTION VALVE(S)
22
DISCHARGE VALVE(S)
23 ROD DIAMETER, mm
24 MAX ALLOW. COMBINED ROD LOADING, kN, C *
25 MAX ALLOW. COMBINED ROD LOADING, kN, T *
26 CALCULATED GAS ROD LOAD, kN, C *
27 CALCULATED GAS ROD LOAD, kN, T *
28 COMBINED ROD LOAD (GAS + INERTIA), kN, C *
29 COMBINED ROD LOAD (GAS + INERTIA), kN, T *
30 ROD REV., DEGREES MIN @ X-HD PIN**
31 RECIP WT. (PISTON, ROD, X-HD & NUTS), kg**
32 MAX ALLOW. WORKING PRESSURE, barg
33 MAX ALLOW. WORKING TEMPERATURE, °C
34 HYDROSTATIC TEST PRESSURE, barg
35 GAS LEAKAGE TEST PRESSURE, barg
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
36 INLET FLANGE SIZE/RATING
37
FACING
38 DISCHARGE FLANGE SIZE/RATING
39
FACING
40 DISCHARGE RELIEF VALVE SETTING DATA AT INLET PRESSURES GIVEN ABOVE:
41
RECOMMENDED SETTING, barg
42
GAS ROD LOAD, kN, C *
43
GAS ROD LOAD, kN, T *
44
COMBINED ROD LOAD, kN, C *
45
COMBINED ROD LOAD, kN, T *
46
ROD REVERSAL, °MIN @ X-HD PIN**
47 NOTE: CALCULATED AT INLET PRESSURES
48
GIVEN ABOVE & RECOMMENDED SETTING.
49
SETTLE-OUT GAS PRESSURE
50
(DATA REQUIRED FOR STARTING)
* C = COMPRESSION
* T = TENSION
**X-HD = CROSSHEAD
51 NOTES/REMARKS:
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
RECIPROCATING COMPRESSOR
(API 618-5TH) DATA SHEET
SI UNITS
JOB NO.
ITEM NO.
REVISION
DATE
PAGE
8
OF
17
103
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
BY
CONSTRUCTION FEATURES
1
2 SERVICE ITEM NO.
3 STAGE
4 CYLINDER SIZE (BORE DIA), mm
5 ROD RUN-OUT: NORMAL COLD VERTICAL
6
(per Annex C)
7 CYLINDER INDICATOR VALVES REQUIRED
8 INDICATOR CONNECTIONS ABOVE 345 bar
9 FLUOROCARBON SPRAYED CYLINDER
MATERIALS OF CONSTRUCTION
10 CYLINDER(S)
11 CYLINDER LINER(S)
12 PISTON(S)
13 PISTON RINGS
14 WEAR BANDS
REQUIRED
2
15 PISTON ROD(S): MATERIAL/YIELD, N/mm
16 THREAD ROOT STRESS @ MACRL * @ X-HD END
17 PISTON ROD HARDNESS, BASE MATERIAL, Rc
18 PISTON ROD COATING
19
X REQUIRED
COATING HARDNESS, Rc
20 VALVE SEATS / SEAT PLATE
21 VALVE SEAT MIN HARDNESS, Rc
22 VALVE GUARDS (STOPS)
23 VALVE DISCS
24 VALVE SPRINGS
25 ROD PRESSURE PACKING RINGS
26 ROD PRESSURE PACKING CASE
27 ROD PRESSURE PACKING SPRINGS
28 SEAL / BUFFER PACKING, DISTANCE PIECE
29 SEAL / BUFFER PACKING, INTERMEDIATE
30 WIPER PACKING RINGS
31 MAIN JOURNAL BEARINGS, CRANKSHAFT
32 CONNECTING ROD BEARING, CRANKPIN
33 CONNECTING ROD BUSHING, X-HD END
34 CROSSHEAD (X-HD) PIN BUSHING
35 CROSSHEAD PIN
36 CROSSHEAD
37 CROSSHEAD SHOES
38 INSTRUMENTATION IN
COLD SIDE
39 CONTACT W/PROCESS GAS
HOT SIDE
40 * MACRL = MAXIMUM ALLOWABLE COMBINED ROD LOAD
41
DISTANCE PIECE(S):
COMPRESSOR CYLINDER ROD PACKING
42
FULL FLOATING PACKING
43
VENTED TO:
44
TYPE A
TYPE B
TYPE C
FLARE @
barg
SUCTION PRESSURE @
ATMOS.
COVERS:
barg
CYLINDER COMPARTMENT:
(Outboard Distance Piece)
NON-LUBE
SOLID METAL
SCREEN
LOUVERED
VENTED TO
barg
PURGED AT
barg
barg
45
FORCED LUBRICATED
46
WATER COOLED,
STAGE(S),
GPM REQ'D
PRESSURIZED TO
47
OIL COOLED,
STAGE(S),
GPM REQ'D
WITH RELIEF VALVE
48
WATER FILTER
49
VENT/BUFFER GAS SEAL PACKING ARR.
PROV.FUTURE WATER/OIL COOLING
50
CONSTANT OR
51
BUFFER GAS PRESSURE,
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
52
TYPE D
REF. FIGURE G-3
(REF. FIG I-1)
FRAME COMPARTMENT:
(Inboard Distance Piece)
VARIABLE DISPOSAL SYSTEM
SPLASH GUARDS FOR WIPER PACKING
barg
VENTED TO
barg
PURGED AT
barg
PRESSURIZED TO
barg
WITH RELIEF VALVE
DISTANCE PIECE MAWP
barg
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
API STANDARD 618
JOB NO.
RECIPROCATING COMPRESSOR
(API 618-5TH) DATA SHEET
SI UNITS
ITEM NO.
REVISION NO.
PAGE
DATE
9
OF
17
BY
CONSTRUCTION FEATURES (CONTINUED)
1
2
FABRICATED CYLINDER, HEADS, & CONNECTION
3
SKETCHES FOR DESIGN REVIEW
OIL WIPER PACKING PURGE
4
BY PURCHASER. (6.15.5.13)
INTERMEDIATE PARTITION PURGE
BUFFER GAS PACKING ARR.
REF: ANNEX I
FIGURES I-1, I-2 & I-3
INERT BUFFER PURGE GAS:
5
N2
VENT, DRAIN, PURGE PIPING BY MFG'R
6
7
Revision
104
COUPLING(S)
LOW-SPEED
8
HI-SPEED
Between Compressor
& Driver or Gear
9
Between Driver &
Gear
V-BELT DRIVE
OTHER
NO
DRIVEN SHEAVE
YES
DRIVE SHEAVE
(COMPRESSOR SHAFT) (DRIVER SHAFT)
RPM (EXPECTED)
10
BY MANUFACTURER
PITCH DIA. (IN.)
11
MODEL
QTY & GROOVE X-SEC.
12
TYPE
POWER TRANSMITT'D
Incl. Belt Losses
13
14
API-671 APPLIES
YES
NO
15
INSPECTION AND SHOP TESTS (REF. 8.1.5)
16
REQ'D
17 *SHOP INSPECTION
DRIVER NAMEPLATE HP RATING
CENTER DISTANCE (IN.)
WITN. OBSER.
QTY, TYPE,
X-SEC., & LENGTH BELTS
18 ACTUAL RUNNING CLEARANCES
BELT SERVICE FACTOR (RELATIVE TO
19 AND RECORDS
DRIVER NAMEPLATE HP RATING)
20 MFG STANDARD SHOP TESTS
CYLINDER LUBRICATION
21 CYLINDER HYDROSTATIC TEST
NON-LUBE
STAGE(S)/SERVICE
22 CYLINDER PNEUMATIC TEST
LUBRICATED
STAGE(S)/SERVICE
23 CYLINDER HELIUM LEAK TEST
TYPE OF LUBE OIL:
SYNTHETIC
24 CYL. JACKET WATER HYDRO TEST
HYDROCARBON
25 *MECHANICAL RUN TEST (4 HOUR)
LUBRICATOR
26 BAR-OVER TO CHECK ROD RUNOUT
DRIVE BY:
COMP. CRANKSHAFT, DIRECT
CHAIN, FROM CRANKSHAFT
27 *LUBE OIL CONSOLE RUN/TEST (4 HOUR)
28 *COOLING H2O CONSOLE RUN/TEST
29 RADIOGRAPHY BUTT WELDS
30
GAS
OIL
ELECTRIC MOTOR
OTHER
LUBRICATOR MFR
FAB CYLS.
MODEL
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
31 MAG PARTICLE/LIQUID
TYPE LUBRICATOR:
SINGLE PLUNGER PER POINT
32
PENETRANT OF WELDS
33
SPECIFY ADDITIONAL
COMPARTM'T, TOTAL QTY.
34
REQUIREMENTS (8.2.1.3)
PLUNGERS (PUMPS), TOTAL QTY.
(6.14.3)
35
DIVIDER BLOCKS
SPARE PLUNGERS, QTY.
36 SHOP FIT-UP OF PULSATION SUPPL.
37
DEVICES & ALL ASSOCIATED
38
GAS PIPING
SPARE COMPARTM'T W/OUT PLUNGERS
HEATERS:
ELECTRIC W/THERM.(S)
STEAM
ESTIMATED WEIGHTS AND NOMINAL DIMENSIONS
39 *CLEANLINESS OF EQUIP., PIPING,
TOTAL COMPR. WT, LESS DRIVER & GEAR
kg
WT, OF COMPLETE UNIT, (LESS CONSOLES)
kg
41 *HARDNESS OF PARTS, WELDS &
MAXIMUM ERECTION WEIGHT
kg
42 HEAT AFFECTED ZONES
MAXIMUM MAINTENANCE WEIGHT
43 *NOTIFICATION TO PURCHASER OF
DRIVER WEIGHT/GEAR WEIGHT
/
kg
44 ANY REPAIRS TO MAJOR
LUBE OIL/COOLANT CONSOLE
/
kg
40
& APPURTENANCES
45 COMPONENTS
kg
FREE STANDING PANEL
46
SPACE REQUIREMENTS, m:
47
COMPLETE UNIT
48 *SPECIFIC REQUIREMENTS TO BE DEFINED,
49 FOR EXAMPLE, DISMANTLING, AUX EQUIPMENT
LUBE OIL CONSOLE
CYLINDER COOLANT CONSOLE
50 OPERATIONAL & RUN TESTS.
FREE STANDING PANEL
51 ANNEX K COMPLIANCE:
VENDOR
52
PURCHASER
LENGTH
WIDTH
HEIGHT
PISTON ROD REMOVAL DIST.
OTHER EQUIPMENT SHIPPED LOOSE (DEFINE)
53
PULSATION SUPP., WEIGHT
kg
54
PIPING
kg
55
INTERSTAGE EQUIPMENT
kg
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
105
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
ITEM NO.
REVISION NO.
PAGE
DATE
10
OF
17
BY
UTILITY CONSUMPTION
1
2
ELECTRIC MOTORS
3
4
5
FOR INDUCTION
6
MOTORS SEE NOTE
7
OF 7.1.2.6 AND
8
MOTOR DATA SHEET
NAMEPLATE
LOCKED ROTOR
FULL LOAD
MAIN DRIVER NON-STEADY
kW
AMPS
STEADY STATE
STATE AMPS AT COMPRES-
AMPS
SOR RATED HORSEPOWER
(INDUCTION MOTORS ONLY)
9
MAIN DRIVER
10
MAIN LUBE OIL PUMP
@ COMPRESSOR RATED
AMPS
11
AUX LUBE OIL PUMP
kW OF
12
MAIN CYLINDER COOLANT PUMP
@ CURRENT PULSATIONS
13
AUX CYLINDER COOLANT PUMP
OF
14
MAIN ROD PKG COOLANT PUMP
15
AUX ROD PKG COOLANT PUMP
16
CYLINDER LUBRICATOR
%
17
18
19
ELECTRIC HEATERS
20
21
WATTS
22
FRAME OIL HEATER(S)
23
CYLINDER COOLANT HEATER(S)
24
CYL. LUBRICATOR HEATER(S)
25
MAIN DRIVER SPACE HEATER(S)
VOLTS
HERTZ
26
27
28
STEAM
29
30
FLOW
PRESSURE
TEMPERATURE
BACK PRESSURE
31
MAIN DRIVER
kg/h @
barg
°CTT TO
32
FRAME OIL HEATER(S)
kg/h @
barg
°CTT TO
barg
barg
33
CYL. LUB. HEATER(S)
kg/h @
barg
°CTT TO
barg
34
kg/h @
barg
°CTT TO
barg
35
kg/h @
barg
°CTT TO
barg
36
COOLING WATER REQUIREMENTS
37
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
38
FLOW
39
m /h
3
40
CYLINDER JACKETS
41
CYLINDER COOLANT CONSOLE
42
FRAME LUBE OIL COOLER
43
ROD PRESSURE PACKING*
44
PACKING COOLANT CONSOLE
45
INTERCOOLER(S)
46
AFTERCOOLER
INLET TEMP
°C
OUTLET TEMP
°C
INLET PRESS
barg
OUTLET PRESS
barg
47
48
3
TOTAL QUANTITY, m /h
49 REMARKS/SPECIAL REQUIREMENTS:
50
*ROD PACKING COOLANT MAY BE OTHER THAN WATER
51
DS 618 10
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
MAX PRESS
barg
API STANDARD 618
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
3
4
ITEM NO.
REVISION NO.
PAGE
DATE
11
OF
17
BY
FRAME LUBE OIL SYSTEM
1
2
Revision
106
SPLASH
BASIC LUBE OIL SYSTEM FOR FRAME:
REF: TYPE MAIN BEARINGS:
PRESSURE SYSTEM:
PRESSURE (FORCED)
TAP'RD ROLL'R
MAIN OIL PUMP DRIVEN BY:
5
HEATERS REQUIRED:
PRECISION SL'VE
ELEC. W/THERMOSTAT(S)
COMP. CRANKSHAFT
ELEC. MOTOR
PSV FOR MAIN PUMP EXTERNAL TO CRANKCASE
6
AUX OIL PUMP DRIVEN BY:
7
HAND OPERATED PRE-LUBE PUMP FOR STARTING
8
CHECK VALVE ON MAIN PUMP (FIG G-5)
ELEC. MOTOR
OTHER
OPERATIONAL TEST & 4 HOUR MECH RUN TEST
CONTINUOUS OIL FLOW THROUGH SWITCH SENSING LINE (7.7.2.5)
9
SEP. CONSOLE FOR PRESS. LUBE SYS:
ONE CONSOLE FOR EA. COMP.
10
Note:
CONSOLE TO BE OF DECK PLATE TYPE CONSTRUCTION SUITABLE FOR
MULTI-POINT SUPPORT AND GROUTING WITH GROUT & VENT HOLES.
11
12
13
14
Instrumentation to be listed on
Instrumentation Data Sheets.
ELECTRICAL CLASSIFICATION : CLASS
LUBE OIL
,
DIV
PRESSURE
barg
3
m /h
COMPRESSOR FRAME
17
DRIVER
COMPRESSORS
NON-HAZARDOUS
VISCOSITY
SSU @ 40°C
SSU @ 100°C
SUMP VOLUME
m
3
GEAR
DESIGN
SYSTEM PRESSURES:
20
21
GROUP
FLOW
16
19
,
ONE CONSOLE FOR
BASIC SYS. REQ'MTS (NORM. OIL FLOWS & VOLUMES)
15
18
STEAM
OTHER
barg
HYDROTEST
PRESSURE CONTROL VALVE SETTING
CARBON
STEEL
PIPING MATERIALS:
22
23
UPSTREAM OF PUMPS & FILTERS
24
DOWNSTREAM OF FILTERS
barg
barg
STAINLESS STEEL
WITH SS FLANGES
PUMP REL'F VALVE(S) SET
barg
STAINLESS STEEL
WITH CARBON STEEL FLANGES
25
26
27
28
PUMPS
(Gear
or Screw Type Only)
29
MAIN
30
AUXILIARY
RAT'D FL'W
m
3
PRESSURE
barg
31
PUMP CASING MATERIAL (Ref. 6.14.2.1.5):
32
GUARD(S) REQ. FOR COUPLING(S):
33
DRIVER
kW
SPEED
R/MIN
MAIN PUMP
MECH. SEAL
REQ'D
AUX PUMP
MAIN PUMP
MANUAL
COUPLING
REQ'D
AUX PUMP
ON-OFF-AUTO SEL. SWITCH:
BY PURCH.
BY MFR.
WIRING TO TERMINAL BOX:
BY PURCH.
BY MFR.
35
SWITCHES
SHELL & TUBE
COOLERS:
SINGLE
AUTOMATIC
GUARD TYPE OR CODE
34
36
AUXILIARY PUMP CONTROL:
COLD START
REQ'D kW
DUAL W/TRANSFER VALVE
MFG'S STD.
TEMA C
TEMA R (API 660)
37
REMOVABLE BUNDLE
38
W/BYPASS & TEMP CONTROL VALVE:
39
SEE SEPARATE HEAT EXCHANGER DATA SHEETS FOR DETAILS, SPECIFY % GLYCOL ON COOLING WATER SIDE
40
SINGLE
FILTER(S)
DESIGN PRESSURE,
42
MICRON RATING,
44
MANUFACTURER
AUTO
ASME CODE DESIGN
' P CLEAN,
barg
ASME CODE STAMPED
barg
CARTRIDGE MATERIAL,
BONNET MATERIAL,
SYS. COMPONENT SUPP.
AIR COOLED W/AUTO TEMP CONTROL (API-661) Data Shts - Attached
MANUAL
DUAL W/TRANSFER VALVE
41
43
WATER COOLED
RTD'S/THERMOCOUPLES
CASING MATERIAL,
MODEL
' P COLLAPSE,
FURN.SPARE CARTR.,QTY
MANUFACTURER
45
MAIN PUMP
OIL COOLER(S)
46
AUXILIARY PUMP
TRANSFER VALVE(S)
47
MECHANICAL SEALS
PUMP COUPLING(S)
48
ELECTRIC MOTORS
SUCTION STRAINER(S)
49
STEAM TURBINES
CHECK VALVE(S)
50
OIL FILTER(S)
51
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
barg
CARTRIDGE P/N
MODEL
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
PAGE
DATE
OF
17
BY
ROD PACKING(S)
HEATERS REQ.'D FOR PRE-HEATING:
OPEN, PIPING BY:
PRESSURE FORCED CIRCULATING SYS:
PROCESS COOLER(S)
ELEC.,W/ THERMOSTAT(S)
PURCH.
MFR
MAIN COOLANT PUMP DRIVEN BY:
ELEC. MOTOR
STEAM TURBINE
OTHER
6
AUX COOLANT PUMP DRIVEN BY:
ELEC. MOTOR
STEAM TURBINE
OTHER
7
SEP. CONSOLE FOR COOLANT SYSTEM.:
8
NOTE:
9
10
11
ONE CONSOLE FOR EA. COMP.
Instrumentation to be listed on
instrumentation data sheets.
14
CYLINDER(S),
STAGE
15
CYLINDER(S),
STAGE
16
CYLINDER(S),
STAGE
17
CYLINDER(S),
STAGE
18
CYLINDER(S),
STAGE
19
CYLINDER(S),
STAGE
20
PISTON ROD PACK'G TOTAL
21
INTERCOOLER(S) TOTAL
22
AFTERCOOLER
23
OIL COOLER(S)
ONE CONSOLE FOR
COMP'RS
MULTI-POINT SUPPORT AND GROUTING WITH GROUT & VENT HOLES.
,
GROUP
,
DIV
NON-HAZARDOUS
COOLANT TO BE
BASIC SYS. REQ'MTS (NORM. COOLANT FLOW DATA)
13
CLOSED, PIPING BY MFR.
CONSOLE TO BE OF DECK PLATE TYPE CONSTRUCTION SUITABLE FOR
ELECTRICAL CLASSIFICATION : CLASS
12
OIL COOLER(S)
STEAM
% ETHYLENE GLYCOL
SITE
FORCED
THERMO
STAND
FLOW
PRESSURE
INLET TEMP
OUTLET TEMP
FLOW
COOL'G
SYPHON
PIPE
m /h
3
barg
°C
°C
IND'TR
24
25
TOTAL FLOW
26
SYS. PRESSURES:
27
COOLANT RESERVOIR:
DESIGN,
barg
SIZE,
HYDROTEST,
mm IN DIA X
barg
mm IN HT.
RELIEF VALVE(S), SETTING
CAPACITY
28
RESERVOIR MATERIAL
30
LEVEL GAUGE
PUMPS: (CENTRIFUGAL ONLY)
32
MAIN
34
AUXILIARY
LEVEL SWITCH
DRIVER
SPEED
3
barg
kW
kW
r/min
PUMP CASING MATERIAL (Ref 6.14.2.1.5):
GUARD(S) REQ.'D FOR COUP'G(S)
MANUAL
MAIN PUMP
MAIN PUMP
AUTO
38
COOLANT HEAT EXCHANGER:
INSPECTION & CLEAN-OUT OPENINGS
REQ'D
36
39
DRAIN VALVE
PRESS.
35
AUX.PUMP CONTROL:
INTERNAL COATING, TYPE
RAT'D FL'W
m /h
33
37
SHELL & TUBE
COUPLING MECH.SEAL
REQ'D
REQ'D
AUX PUMP
AUX PUMP
GUARD TYPE OR CODE
ON-OFF-AUTO SEL. SWITCH:
BY PURCH.
WIRING TO TERMINAL BOX:
BY PURCH.
SINGLE
DUAL W/TRANSFER VALVE
BY MANUFACTURER
BY MANUFACTURER
TEMA C
40
TEMA R (API 660)
(DATA SHEETS ATTACHED)
41
AIR COOLED EXCHANGER W/AUTO TEMP CONTROL (API 661 DATA SHEETS ATTACHED)
42
W/BYPASS & TEM. CONTROL VALVE
43
SEE SEPARATE COOLER DATA SHEET FOR DETAILS; SPECIFY % GLYCOL ON BOTH SIDES
MANUAL
AUTO
LOUVERS FOR AIR EXCH.
OF SHELL & TUBE
44
45
barg
3
@ NORMAL OPERATING LEVEL
29
31
m
SYS. COMPONENT SUPP.
MANUFACTURER
MODEL
MANUFACTURER
46
MAIN PUMP
TEMP CONTROL VALVE(S)
47
AUXILIARY PUMP
TRANSFER VALVE(S)
48
MECHANICAL SEALS
PUMP COUPLING(S)
49
ELECTRIC MOTORS
50
STEAM TURBINES
51
52
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
MODEL
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
4
12
COOLANT SYSTEM
COMPRESSOR CYL.(S)
BASIC COOLING SYS. FOR:
3
5
ITEM NO.
REVISION NO.
1
2
107
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
API STANDARD 618
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
Revision
108
ITEM NO.
REVISION NO.
PAGE
DATE
13
OF
17
BY
1
PULSATION SUPPRESSION DEVICES FOR RECIPROCATING COMPRESSORS
2
THESE SHEETS TO BE FILLED OUT FOR EACH SERVICE AND/OR STAGE OF COMPRESSION
3 APPLICABLE TO:
PROPOSALS
PURCHASE
AS BUILT
4 FOR/USER
5 SITE/LOCATION
AMBIENT TEMPERATURE MIN/MAX
6 COMPRESSOR SERVICE
NUMBER OF COMPRESSORS
7 COMPRESSOR MFG.
MODEL/TYPE
/
°C
8 SUPPRESSOR MFG.
9 NOTE:
Ind.Data Comp.'d Purch.
By Compr/Supp.Mfg.w/Proposal
By Mfg(s) after order
By Mfg(s)/Purchaser as Applicable
GENERAL INFORMATION APPLICABLE TO ALL SUPPRESSORS
10
11 TOTAL NUMBER OF SERVICES AND/OR STAGES
12 TOTAL NUMBER OF COMPRESSOR CYL.
TOTAL NUMBER OF CRANKTHROWS
13
ASME CODE STAMP
14
OTHER APPLICABLE PRESSURE VESSEL SPEC. OR CODE
15
LUBE SERVICE
16
RADIOGRAPHY (X-RAY OF WELDS):
17
SHOP INSPECTION
18
STROKE
GOVERNMENTAL CODES OF
NON-LUBE SERV.
WITNESSED
NO OIL ALLOWED INTERNALLY
NONE
WITNESS HYDROTEST
SPOT
mm
r/min
CODE REGULATIONS APPLY
100%
DRY TYPE INTER.CORR.COATING
IMPACT TEST
YES
NO
SPECIAL WELDING REQUIREMENTS
OUTDOOR STORAGE OVER 6 MONTHS
SPECIAL PAINT SPEC
OBSERVED
19
CYLINDER, GAS, OPERATING, AND SUPPRESSOR DESIGN DATA
20
21
SERVICE
STAGE NO.
22
COMPRESSOR MANUFACTURER'S RATED CAPACITY
23
LINE SIDE OPERATING PRESSURE
INLET,
bar
DISCHARGE,
24
OPERATING TEMP. WITHIN SUPPRESSORS
INLET,
°C
DISCHARGE,
25
ALLOWABLE PRESSURE DROP THROUGH SUPPRESSORS
26
LBS/HR
SCFM
'P
bar
MMSCFD
/
%
INLET SUPPRESSOR
27
SUPRESSOR TAG NUMBER
28
COMBINATION INLET SUPP SEPARATOR/INTERNALS
29
NO. (QTY) OF INLET & DISCH. SUPP. PER STAGE
YES
NO
/
'P
bar
°C
bar
/
%
DISCHARGE SUPPRESSOR
YES
/
NO
YES
NO
30
ALLOWABLE PEAK-PEAK PULSE @ LINE SIDE NOZZLE
bar
/
%
bar
/
%
31
ALLOWABLE PEAK-PEAK PULSE @ CYL FLANGE NOZZLE
bar
/
%
bar
/
%
32
33
DESIGN FOR FULL VACUUM CAPABILITY
34
MIN. REQ'D WORKING PRESSURE & TEMPERATURE
35
NOTE:
NO
YES
NO
After design, the actual MAWP & temp are to be determined
36
based on the weakest component and stamped on the
37
vessel. The actual MAWP is to be shown on pg.14 line 12
38
YES
barg,
@
°C
barg,
@
°C
and on the U1A Forms.
39
INITIAL SIZING VOL. PER FORMULA OF 7.9.3.2
40
NOTE:
This is a Reference
m
3
m
3
41
42
AS BUILT VOLUME (m³)
m
3
43
44
45
46
47
48
49
50
51
52
DS 618 13
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
m
3
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
ITEM NO.
REVISION NO.
PAGE
DATE
14
OF
17
BY
1
PULSATION SUPPRESSION DEVICES FOR RECIPROCATING COMPRESSORS (CONT'D)
SERVICE
2
THESE SHEETS TO BE FILLED OUT FOR EACH SERVICE AND/OR STAGE OF COMPRESSION
STAGE NO.
INLET SUPPRESSOR
3 CONSTRUCTION REQUIREMENTS & DATA
4
SUPRESSOR TAG NUMBER
5
BASIC MATERIAL REQUIRED, CS, SS, ETC.
6
ACTUAL MATERIAL DESIGNATION
SHELL/HEAD
7
SPECIAL HARDNESS LIMITATIONS, Rc
YES
8
CORROSION ALLOWANCE., mm
WALL THICKNESS, mm
11
PIPE OR ROLLED PLATE CONSTRUCTION
12
ACT. MAX ALLOW. WORKING PRESS. AND TEMPERATURE
13
MINIMUM DESIGN METAL TEMP (6.15.8.1)
14
INLET SUPRESS. TO BE SAME MAWP AS DISCH'RGE SUPPRESS.
15
MAX EXPECTED PRESSURE DROP(¨ P, %) LINE PRESS
16
WEIGHT (kg EACH)
SHELL/HEAD
(INCH/VOL.mm³)
x
20
SUPPORTS, TYPE/QUANTITY
22
LINE SIDE FLANGE.
23
COMP CYL FLANGE(S), QTY/SIZE/RATING/FACING/TYPE
24
FLANGE FINISH,
PER 7.9.5.1.16
>125 <250
26
INSPECTION OPENINGS REQUIRED
PIPE
°C
YES
3
ROLLED PLATE
bar @
°C
°C
NO
bar/
%
' P
bar/
%
%/
kg
%
%/
%
PER ANSI 16.5
YES
NO
BLINDED
YES
NO
BLINDED
SPEC. QTY. SIZE, /FLG TYPE & RATING
* QTY. SIZE, /FLG TYPE & RATING
VENT CONNECTIONS REQUIRED
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
YES
NO
YES
NO
YES
NO
YES
NO
YES
NO
YES
NO
YES
NO
YES
NO
SPEC. QTY. SIZE, /FLG TYPE & RATING
* QTY. SIZE, /FLG TYPE & RATING
DRAIN CONNECTIONS REQUIRED
SPEC. QTY. SIZE, /FLG TYPE & RATING
* QTY. SIZE, /FLG TYPE & RATING
PRESSURE CONNECTIONS REQUIRED
SPEC. QTY. SIZE, /FLG TYPE & RATING
* QTY. SIZE, /FLG TYPE & RATING
38
TEMPERATURE CONNECTIONS REQUIRED
39
SPEC. QTY. SIZE, /FLG TYPE & RATING
41
mm
mm
SPECIAL (SPECIFY)
37
40
ROLLED PLATE
mm/
mm/
SIZE/RATING/FACING/TYPE
25
36
x
CONNECTION REQUIREMENTS & DATA
21
35
3
kg
19
34
mm
'P
INSUL NUTS & ALLOW. FOR INSULATION REQUIRED (X)
33
WELDS
°C
EXPECTED P-P PULSE @ LINE SIDE/CYL FLG, % LINE PRESS
BASED ON FINAL SUPPRESSOR DESIGN
32
mm
mm/
bar @
17
31
SHELL & HEADS
mm
mm/
PIPE
18
30
WELDS
mm
NOM. SHELL DIA X OVERALL LGTH.
29
/
SHELL & HEADS
REQUIRED
9
28
DISCHARGE SUPPRESSOR
/
NO
10
27
109
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
CYL NOZZLE
MAIN BODY
* QTY. SIZE, /FLG TYPE & RATING
42
43
44
45
OTHER DATA AND NOTES
46
47
COMPRESSOR MFG'S SUPP. OUTLINE OR DRAWING NO.
48
SUPP. MFG'S OUTLINE OR DRAWING NO.
49
NOTES * = AS BUILT
50
51
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
JOB NO.
ITEM NO.
REVISION NO.
DATE
PAGE
15
OF
17
Revision
110
BY
INSTRUMENTATION
1
2 PURCHASER TO FILL IN
(
) AFTER COMMODITY TO INDICATE:
3
INSTRUMENT & CONTROL
ONE FOR EA. UNIT
4
PANEL
MACHINE MT'ED
(
):
BY COMP. MFR.
BY PURCH.
BY OTHERS
REMOTE
OUTDOORS
ONE COMMON TO ALL UNITS
FREE STANDING (OFF UNIT)
ELEC.
ELECTRONIC
LOCAL
5
PNEUMATIC
HYDRAULIC
6
NEMA 7, CLASS
, GROUP
7
I/S BARRIERS (
)
8
NEMA 4, WATERTIGHT & DUSTTIGHT
9
OTHER NEMA
10
VIB, ISOLATORS
11
ANNUNCIATOR W/FIRST-OUT INDICATION LOCATED ON CONTROL PANEL
, DIVISION
PROGRAMMABLE CONTL'R
INTRINSICALLY SAFE
PURGED TO NFPA 496 TYPE
LOW PURGE PRESS.
STRIP HEATERS
X
ALARM
PURGE CONN.
Y
Z
SHUTDOWN
EXTRA CUTOUTS
PURCHASER'S CONN. BROUGHT OUT TO TERMINAL BOX BY VENDOR
12
13
BUFFER GAS CONTROL
14
PANEL
(
):
ONE FOR EA. UNIT
ONE COMMON TO ALL UNITS
MACHINE MT'ED
FREE STANDING (OFF UNIT)
15
CLASS
, GROUP
16
CONSTANT PRESSURE DISPOSAL SYSTEM
WITH STAND
OUTDOORS
, DIVISION
VARIABLE PRESSURE DISPOSAL SYSTEM
17 ADDITIONAL PANEL REMARKS:
18
19
20
INSTRUMENTATION SUITABLE FOR:
21
PREFERRED INSTRUMENT SUPPLIERS, (TO BE COMPLETED BY PURCHASER), OTHERWISE MFR'S STANDARD APPLIES
INDOORS
OUTDOORS
OTHER
22
PRESSURE GAUGES
MFR
SIZE & TYPE
MTL
23
TEMPERATURE GAUGES
MFR
SIZE & TYPE
MTL
24
LIQUID LEVEL GAUGES
MFR
25
DIFF. PRESSURE GAUGES
MFR
26
PRESS. TRANSMITTERS
MFR
TYPE
27
LIQUID LEV. TRANSMITTER
MFR
TYPE
MTL
28
PRESSURE SWITCHES
MFR
TYPE
MTL
29
TEMPERATURE SWITCHES
MFR
TYPE
MTL
30
LIQUID LEVEL SWITCHES
MFR
TYPE
MTL
31
DIFF. PRESSURE SWITCHES
MFR
TYPE
MTL
32
CONTROL VALVES
MFR
TYPE
MTL
33
PRESSURE SAFETY VALVES
MFR
TYPE
MTL
34
SIGHT FLOW INDICATORS
MFR
TYPE
MTL
35
VIBRATION MONITORS & EQUIP.
MFR
TYPE
MTL
36
THERMOCOUPLES
MFR
TYPE
MTL
37
RTD'S
MFR
TYPE
MTL
38
SOLENOID VALVES
MFR
TYPE
MTL
39
ANNUNCIATOR
MFR
40
PROGRAMMABLE CONTROLLER
MFR
41
42
TYPE
MTL
MTL
(
MODEL & (QTY SPARE POINTS)
TYPE
MFR
PRESSURE GAUGE REQUIREMENTS
MTL
SIZE & TYPE
TYPE
LIQUID-FILLED PRESSURE GAUGES:
)
MTL
MTL
YES
NO
43
LOCALLY
PANEL
LOCALLY
PANEL
44 FUNCTION
MOUNTED
MOUNTED
MOUNTED
MOUNTED
45
LUBE OIL MAIN PUMP DISCHAR.
(
)
(
)
PROCESS GAS: INLET PRESS.
(
)
(
)
46
LUBE OIL AUX. PUMP DISCHARG.
(
)
(
)
@ EA. STAGE
(
)
(
)
47
LUBE OIL PRESS. AT FRAME HEADER (
)
(
)
DISCH. PRESS.
(
)
(
)
48
LUBE OIL FILTER ' P
(
)
(
)
@ EA. STAGE
(
)
(
)
49
COOLING H2O INLET HEADER
(
)
(
)
(
)
(
)
(
)
(
)
(
)
(
)
50
51 REMARKS:
52
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
JOB NO.
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
ITEM NO.
REVISION NO.
PAGE
DATE
16
OF
17
BY
INSTRUMENTATION (CONT'D)
1
2 TEMPERATURE MEASUREMENT REQUIREMENTS
LOCALLY
PANEL
3 FUNCTION
MOUNTED
MOUNTED
GAUGE W/
4
LUBE OIL
INLET TO
OUT OF
FRAME
(
)
(
)
5
LUBE OIL
INLET TO
OUT OF
COOLER
(
)
(
)
6
MAIN JRNL BEARINGS (THERMOCOUPLES OR RTD'S ONLY)
(
)
(
)
7
MOTOR BEARING(S)
(
)
(
)
(THERMOCOUPLES OR RTD'S ONLY)
8
CYL. COOLANT MANIFOLD:
9
CYL. JKT. COOLANT:
INLET
INLET
OUTLET
OUTLET
EA. CYL
(
)
(
)
(
)
(
)
10
PROCESS GAS:
INLET
DISCH.
EACH CYL
(
)
(
)
11
INTERCOOLER(S)
INLET
GAS
COOLANT
(
)
(
)
OUTLET
GAS
COOLANT
(
)
(
)
AFTERCOOLER:
INLET
GAS
COOLANT
(
)
(
)
OUTLET
GAS
COOLANT
PKG COOLANT
INLET
OUTLET
12
13
14
15
(
)
(
)
(
)
(
)
16
PRESS. PGK CASE, CYL PIST ROD (THRM'CPLS OR RTD'S ONLY)
(
)
(
)
17
COMPRESSOR VALVES
(
)
(
)
18
(
)
(
)
19
(
)
(
)
20
SUCT.
DISCH. TC'S OR RTD'S ONLY
ALARM DEVICES:
TRANSMITTER
SWITCH
23
SHUTDOWN DEVICES
TRANSMITTER
SWITCH
I/S
SYS
SYS
ALARM
25
ALARM
FUNCTION
IN CTL
IN
IN CTL
TOTAL
PNL
ROOM
PNL
ROOM
NO.
SHUT
BY
PANEL
BY
PANEL
OF
DOWN
MFR
OTH'RS
MFR
OTH'RS
POINTS
27
LOW LUBE OIL PRESS. @ BEARING HEADER
(
) (
)
28
HIGH LUBE OIL ' P AP ACROSS FILTER
(
) (
)
29
LOW LUBE OIL LEVEL, FRAME
(
) (
)
30
AUX LUBE OIL PUMP, FAIL TO START
(
) (
)
31
CYL LUBE SYSTEM PROTECTION
(
) (
)
32
COMPR. VIBRATION, SHUTDOWN ONLY
33
VIBRATION, W/ CONTINUOUS MONITORING
34
35
(
)
(
) (
)
ROD DROP DETECTOR, CONTACT TYPE(1/CYL)
(
) (
)
ROD DROP PROXIMITY PROBE (1/CYL)
(
) (
)
36
OIL TEMP OUT OF FRAME
(
) (
)
37
HIGH GAS DISCH. TEMP EACH CYLINDER
(
) (
)
38
HIGH JACKET COOLANT TEMP., EA. CYL
(
) (
)
39
LOW SUCTION PRESS., FIRST STG INLET
(
) (
)
40
HI DISCH. PRESS.
(
) (
)
41
HI CYL. GAS ' P, EACH STAGE
(
) (
)
42
HI LIQ. LEV., EA. MOISTURE SEPARATOR
(
) (
)
43
LOW PURGE GAS PRESS, DISTANCE PIECE(S)
(
) (
)
44
HI X-HD PIN TEMP
(
) (
)
45
PRESS PKG CASE (PISTON ROD TEMP)
(
) (
)
(
) (
FINAL
46
EA STG
47
SHUTDOWN
IN
24
)
TOTAL NUMBER OF ANNUNCIATION POINTS
48
SWITCH CONTACT OPERATION
49
ALARM CONTACTS SHALL:
50
52
RTD
ANNUNCIATION POINTS
22
51
THERMO
CAPILLARY CPL SYS
NOTE: ALARM & SHUTDOWN DEVICES SHALL BE INDIVIDUALLY SEPARATE
ALARM & SHUTDOWN SYSTEM REQ'MTS
21
26
111
Revision
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
NOTE: EACH SWITCH SHALL BE MINIMUM SPDT ARRANGEMENT
OPEN ( DE-ENER.) TO SOUND ALARM & BE ENERGIZED WHEN COMPR. IS IN OPERATION
CLOSE (ENERGIZE) TO SOUND ALARM & BE DE-ENERGIZED WHEN COMPR. IS IN OPERATION
SHUTDOWN CONTACTS SHALL:
OPEN ( DE-ENERGIZED) TO SHUTDOWN & BE ENERGIZE WHEN COMPR. IS IN OPERATION
CLOSE (ENERGIZE) TO SHUTDOWN & BE DE-ENERGIZE WHEN COMPR. IS IN OPERATION
53 REF: 7.6.6.2 FOR MINIMUM RECOMMENDED PROTECTION REQUIREMENTS
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
API STANDARD 618
RECIPROCATING COMPRESSOR
API 618 5TH EDITION DATA SHEET
SI UNITS
3
ITEM NO.
REVISION NO.
DATE
PAGE
SIGHT FLOW IND. (COOLANT ONLY)
(
)
FOR:
PNEUMATIC PRESSURE TRANSMITTERS
(
)
FOR:
6
PRESSURE TRANSMITTERS (ELEC. OUTP.)
(
)
FOR:
7
PNEUMATIC LEVEL TRANSMITTERS
(
)
8
ALARM HORN & ACKN'LMT TEST BUTTON
(
)
9
CONDUIT & WIRING W/JUNCT. BOXES
(
)
10
TEST VALVES
(
)
FOR:
11
DRAIN VALVES
(
)
FOR:
12
GAUGE GLASS(ES)
(
)
FOR:
13
TACHOMETER
(
)
14
CRANKSHAFT KEY PHASER
(
)
15
AND TRANSDUCER
(CONSOLES)
(
16
INTERCOOLER(S)
AFTER CLR
OIL COOLER
ROD PRESS. PKG COOLANT
SPEED RANGE
TO
(
)
(
)
20
(
)
21
(
)
22
(
)
23
(
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
SEPARATE COOLING WATER CONSOLE INSTRUMENT:
)
PURCH. TO LIST REQ'MTS IN ADDITION TO ANY ABOVE REQ'MTS
25
(
)
26
(
)
27
(
)
28
(
)
29
(
)
30
(
)
RELIEF VALVES
LOCATION
32
BY
MANUFACTURER
33
(
)
34
(
)
35
(
)
36
(
)
37
(
)
38
(
)
39
(
)
40
(
)
41
(
)
42
(
)
NOTES:
TYPE
SIZE
SEE MOTOR DATA SHEET FOR ADDITIONAL MOTOR INSTRUMENTATION REQUIREMENTS
44
FOR TURBINE DRIVERS USE APPLICABLE API DATA SHEETS
45
FOR GEAR REDUCERS USE APPLICABLE API DATA SHEETS
46
ELECTRICAL & INSTRUMENTATION CONNECTIONS SHALL BE MADE DIRECTLY BY THE PURCHASER TO INDIVIDUAL
47
48
r/min
FOR:
)
19
43
BY
PURCH. TO LIST REQ'MTS IN ADDITION TO ANY ABOVE REQ'MTS
SEPARATE LUBE OIL CONSOLE INSTRUMENTATION:
18
31
17
CYL JACKET COOLANT
5
24
OF
MISCELLANEOUS INSTRUMENTATION
4
17
17
INSTRUMENTATION (CONT'D)
1
2
JOB NO.
Revision
112
INSTRUMENTS ON THE COMPRESSOR
ADDITIONAL INSTRUMENTATION REMARKS/SPECIAL REQUIREMENTS:
49
50
51
Figure A-2—Reciprocating Compressor Data Sheet (SI Units) (continued)
SETTING
Annex B
(informative)
Capacity Rating and Tolerance
The content of this informative annex refers to 3.18, 3.30, 3.48, 6.13, and 6.1.18.
This annex discusses capacity sizing of reciprocating compressors and the intent of the term “no negative tolerance (NNT)” as
used in this standard to apply to the “normal capacity” of reciprocating process compressors.
The “normal operating point” is defined by the purchaser and is normally the minimum capacity at the specified pressures and
temperatures required to meet the process conditions with no negative tolerance permitted (this is typically the process flow sheet
material balance capacity). The purchaser must complete the data sheets with a capacity, and identify the operating conditions as
“normal” or “alternate.” The purchaser must also provide information on the data sheets about any proposed alternate operating
conditions. The sizing of the compressor must take into account all specified operating conditions, and the manufacturer’s
standard tolerances so that the resulting full-load capacity will never be less than the capacity at the certified operating point.
The compressor “manufacturer’s rated capacity” is that capacity to which the compressor is sized by the manufacturer. The
acceptable standard reciprocating compressor industry tolerance of ±3% is applicable to both the capacity and power at the
compressor shaft. Because of this tolerance on capacity, the manufacturer typically will increase the normal capacity by 3% prior
to sizing the compressor. Frequently, the normal capacity divided by 0.97 equals the manufacturer’s rated capacity. However, due
to the alternate operating conditions, in some cases the manufacturer’s rated capacity may be higher. Since this standard
establishes tolerances on normal capacity, and not the manufacturer’s rated capacity, the purchaser and the manufacturer should
ensure that they have a mutually understood tolerance on the manufacturer’s rated capacity.
“Total power at the compressor shaft,” as used in the data sheets under the manufacturer’s rated capacity, is intended to mean the
power required at the compressor input shaft.
“Total power including power transmission losses” is the total power at the compressor shaft plus all losses in the drive system
and is used for selecting the driver.
The tolerance on the manufacturer’s certified shaft power is ±3% and is calculated on the basis of manufacturer’s rated capacity.
Using the manufacturer’s rated capacity and corresponding power, the proper relationship of power to unit capacity exists and
will agree with calculations. (For example kilowatts per hundred cubic meters per hour or brake horsepower per hundred cubic
feet per minute).
113
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex C
(informative)
Piston Rod Runout
This annex describes a procedure that can be used to determine expected piston rod runout in horizontal reciprocating
compressors with traditional crosshead/piston rod/piston construction. Piston rod runout, using precision dial indicators, is a
measurement criterion used to determine piston rod running alignment variations in both horizontal and vertical positions relative
to cylinder and crosshead alignment. While other alignment methods, such as optical, laser, or wire, may be used to determine
initial assembly alignment, use of dial indicators on the piston rod verifies alignment by determining the true running variation of
the rod as it passes through its stroke. Once factory alignment has been verified by correct rod runout measurement, and so
recorded, it is a convenient field method of verifying alignment after installation and routine maintenance.
Manufacturers with other types of compressors, having unique or proprietary construction, may require different methods for
calculating expected cold vertical rod runout.
C.2 Definition
Piston rod runout is defined in 3.40.
C.3 Maximum Allowable Runout
C.3.1 Acceptable limits of rod runout and shop test requirements and records are discussed in 6.1.28.
C.3.2 The maximum allowable horizontal runout at any side position of the dial indicators shall be zero, plus or minus
0.00015 mm/mm (0.00015 in./in.) of stroke, up to a maximum of 0.064 mm (0.0025 in.).
C.3.3 The maximum allowable vertical runout at any top position of the dial indicators shall be the calculated runout, in
millimeters (thousandths of an inch), at that specific dial indicator position based on length of stroke, length of rod, rod sag, and
the difference between the crosshead and cylinder running clearances, plus or minus a permissible limit of ±0.015% of stroke to
allow for geometric and fit tolerances of all parts that may contribute to slight parallel offset and angular misalignment.
See remainder of this annex for an example of vertical runout calculations based on a suggested procedure.
C.4 General
C.4.1 Piston rod runout is always an inspection requirement during the shop assembly of a new compressor to verify alignment.
It is almost always a purchaser’s witness test requirement of alignment to determine that geometric and fit dimensions of all parts
are correct, and that these parts have been properly assembled with parallel offset and/or angular misalignment within the
established runout limits. In addition, as part of new compressor field installations, rod runout is always checked and verified
against shop readings. It is also a requirement of normal compressor maintenance, especially after overhaul and reassembly of the
cylinders.
C.4.2 Runout must be checked in both horizontal and vertical directions. It is best to check runout at both the crosshead and at
the cylinder to verify that the crosshead and piston are running true in the crosshead guide and cylinder respectively.
C.4.3 While rod runout can be used to verify alignment, it should not be used to align compressor cylinders during the original
assembly of the machine. If the measured cold runout exceeds the expected value, actual running clearances and the runout
calculation should be checked. It is also recommended that all assembled components and fits be checked to confirm they are
within the tolerances required for size, squareness, parallelism, and concentricity.
C.4.4 After assembly and in the field, compressor cylinders, distance pieces, and crosshead guides should never be forced into
positions of harmful stresses in an attempt to satisfy rod runout requirements.
C.4.5 Due to the piston rod length, vertical runout must include the effect of rod sag when type B, C, and D distance pieces are
used. In the case of older units, or new units with no distance piece, or with the very short type A distance piece, rod sag may be
so minimal that it can be ignored and the basics of Figures C-1 and C-2 can be used to compute expected vertical rod runout for
perfect alignment.
115
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
C.1 Scope
116
API STANDARD 618
Rod length 2800 mm (110 in.)
Stroke 280 mm (11 in.)
(0.080 in.)
Cold running
clearance
2 mm
0.50 mm (0.020 in.) Crosshead clearance
0.25 mm (0.010 in.)
0.25 mm
(0.010 in.)
1 mm (0.040 in.)
C Bore centerline
Piston drop
below centerline
bore due to
clearance
76 mm (3 in.) Rod diameter
Crosshead
centerline
Crosshead
Piston
Crosshead
guide
0.75 mm
(0.030 in.)
$ DROP
Cylinder
Figure C-1—Basic Geometry with Cold Vertical Runout
Vertical rod runout at perfect alignment conditions,
with no rod sag, closely approximates a
proportional right triangle relationship where
280 mm (11 in.)
Stroke
Runout
Crosshead
face
Stroke
Rod Length
0.75 mm (0.030 in.)
$ DROP
Piston ro
d
Runout
Piston
end
0
Dial
indicator
Runout
$ DROP
Stroke
Rod Length
X
$ DROP
$ DROP 1/2 difference in running clearance
of piston and crosshead
Piston ro
d
Runout
0.075 mm (0.003 in.)
Stroke
11
110
X
0.030
0.003 in. for this example
Or 280
2800
X
0.75
0.075 mm for this example
Piston ro
d
Figure C-2—Vertical Runout Geometric Relationships Based on No Rod Sag
C.5 Procedure
C.5.1 Rod runout should ideally be checked at both the crosshead end and at the piston end of the rod. For this purpose one dial
indicator is placed as close as possible to the crosshead and the other is placed as close as possible to the piston, the latter position
being in the distance piece next to the rod pressure packing case as shown in Figure C-6A. This is about as close to the piston and
cylinder as typically attainable. Normally checks are made in the cold condition, that is, when all parts are at ambient temperature.
C.5.2 Factory readings are to be recorded on a “runout table” similar to that illustrated in Figure C-3 and provided as part of the
manual for rod runout reference at time of installation.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Rod length 2800 mm (110 in.)
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
117
2/$ 25./54 4!",%
#ONTRACTOR5SER
*OB .O
0URCHASE /RDER .O
3ITE,OCATION
#OMPRESSOR -FGR
4YPE-ODEL
0ISTON 2OD 2UNOUT $ATA 4HROW .O
$ATE
3ER .O
3TAGE
#YL "ORE $IA
#YLINDER "ORE 2UNNING #LEARANCE
2EF 2OD $IA
)TEM .O
#ROSSHEAD 2UNNING #LEARANCE
2OD ,ENGTH #ROSSHEAD &ACE TO #% 0ISTON &ACE
)NDICATOR 0OSITIONS 0ISTON AT #% &ROM #ROSSHEAD &ACE 4O
8
#
2OD
8
2OD 3AG
#
%80%#4%$ !#45!, 2/$ 25./54
)NDICATORS
#ROSSHEAD
&ACE
3TROKE
#%
0ISTON
!LLOWABLE
,IMITS 8
%XPECTED
-EASURED
6ALUES 8
!CTUAL
!LLOWABLE
,IMITS #
%XPECTED
#OLD "EFORE 2UN
6ERTICAL
4OP .UT ,OOSE
(ORIZONTAL
$RIVE 3IDE .UT ,OOSE
6ERTICAL
4OP .UT 4IGHT
(ORIZONTAL
$RIVE 3IDE .UT 4IGHT
(OT !FTER RUN
5NIT .OT 3HOP 2UN
6ERTICAL
4OP
(ORIZONTAL
$RIVE 3IDE
#OLD 2ETAKE
2EQUIRED
.OT 2EQUIRED
6ERTICAL
4OP
(ORIZONTAL
$RIVE 3IDE
Figure C-3—Rod Runout Table
-EASURED
6ALUES #
!CTUAL
)NSPECTOR
$ATE
--``,,,``,,`````,`
118
API STANDARD 618
C.5.3 Dial indicators for vertical runout should be placed on top of the rod at the twelve o’clock position as shown in Figure
C-4, Figure C-5, and Figure C-6A. For horizontal runout, dial indicators should be placed on the “drive side” (in other words,
the side toward the driver) of the rod at the three o’clock or nine o’clock position depending on which throw is being
measured. For accurate readings, dial indicators must be perpendicular to the rod at these positions.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
119
A 110 in.
B 95 in.
C 80 in.
X 14 in.
Dial
indicators
Cylinder
0
D
0
Piston
0.0074 in. Max deflection
@ 0.4215 x 95 in.
Crosshead
Dial indicator at
packing case
40 in.
Crosshead and cylinder clearances identical, $ DROP 0
11 in.
Stroke
C 69 in.
Cylinder
-0.0022 in.
.0031 in.
3 in. Diameter rod
Piston
Note: This example is based
on US customary units.
Initial deflection calculation:
Crosshead end supported (free end) - piston end fixed.
Max deflection occurs at 0.4215 x rod length 95 in.
Rod diameter = 3 in.
Density = 0.283 lb/in3 (steel)
Modulus of elasticity, E = 30 x 106 psi
Rod length B = 95 in.
Max D =
1
184.65
WB3
EI
=
Total weight = 190 lb
Moment of inertia, I = 3.9761 in.4
Rod length C at cylinder indicator position = 80 in.
190 X 953
30 X 106 X 3.9761
1
184.65
1
48
×
W
EIB
= 0.0074 in. at 40.04 in. from free end
(3BC3 - 2C4 - B3C)
Deflection at any point C on the rod
=
Deflection at indicator location C = 80 in.
=
Deflection at C = 69 in. (80 in. minus stroke)
= 0.02083 × 1.6767 × 10-8 (3 X 95 X 693 - 2 × 694 - 953 × 69)
= 0.02083 × 1.6767 × 10-8 (-10,868,052) = -0.0038 in.
190
1
×
(3 × 95 × 803 - 2 × 804 - 953 × 80)
EI × 95
48
= 0.02083 × 1.6767 × 10-8 (-4,590,000) = -0.0016 in.
Rod runout at packing case = 0.0016 in. - 0.0038 in. = -0.0022 in.
The same calculations for the indicator location of 14 in. from the crosshead and at 3 in. after stroking 11 in. gives a
value of +0.0031 for rod runout at the crosshead.
Figure C-4—Rod Runout Attributable to Piston Rod Sag with U DROP = 0
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
X 3 in. After stroking for runout
Crosshead
120
API STANDARD 618
B 95 in.
C 80 in.
X 14 in.
Cylinder
Dial
indicators
0.080 in. Clearance
D
0
0
$ DROP 0.030 in.
Rod
Crosshead
Piston
0.020 in. Crosshead clearance
Dial indicator at
packing case
Crosshead clearance = 0.020 in., cylinder clearance = 0.080 in., $ DROP 0.030 in.
11 in.
Stroke
Cylinder
C 69 in.
.0061 in.
0.080 in. Clearance
+0.0008 in.
$ DROP 0.030 in.
Rod
X 3 in. After stroking for runout
Piston
Crosshead
Note: This example is based
on US customary units.
D = Maximum sag
To calculate rod runout at cylinder running clearances that are different than the crosshead running clearance, combine the
deflection runout shown for Figure C-4 with incremental $ DROPS at indicator positions based on Figure C-2. These calculations can
be quite extensive and are best done by a suitable computer program. A printout of an example of one such program is illustrated
in Figure C-6C using the calculation data shown on Figure C-6B. This particular program calculates the runout values at increments
of 1 in. rod lengths, combines the values, calculates the expected runout figures at the indicator positions, and plots the curves
shown in Figures C-7 through C-11.
As shown on the computer printout sheet Figure C-6C and the curve of Figure C-7, the combined rod runout would be +0.0008 in.
at the packing case indicator location, and +0.0061 in. at the crosshead indicator location with a cylinder running clearance of 0.080
in., and a crosshead running clearance of 0.020 in. for a $ DROP of 0.030 in. The effect of decreasing cylinder running clearance by
0.020 in. increments is also shown on Figure C-6C and the curves of Figure C-8 through C-11. As mentioned in C.9, this is equivalent
to removing 0.010 in. of shims from the bottom shoe of the crosshead, changing the $ DROP by 0.010 in. increments. Note that
each 0.010 in. shim removal changes the rod runout by only about 0.001 in. for this example.
Figure C-5—Rod Runout Attributable to Piston Rod Sag with U DROP > 0
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
A 110 in.
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
2OD LENGTH !
)NNER FACE OF CROSSHEAD NUT
0ISTON LENGTH
2OD LENGTH "
2OD LENGTH #
,ENGTH 8
$IAL
INDICATORS
0ACKING CASE
#ROSSHEAD RUNNING
CLEARANCE
121
#%
HEAD
#YLINDER RUNNING
CLEARANCE
TO TOP OF RING
0ISTON
0ISTON ROD
#ROSSHEAD
#ROSSHEAD GUIDE
3TROKE
#YLINDER
2IDER RINGS
4HROW NUMBER
3TAGE
#YLINDER BORE DIAMETER
#YLINDER RUNNING CLEARANCE
#ROSSHEAD RUNNING CLEARANCE
3TROKE
2OD DIAMETER
2OD LENGTH !
2OD LENGTH "
2OD LENGTH # )NDICATOR 0OSITION
2OD LENGTH 8 )NDICATOR 0OSITION
2OD MATERIAL
-ATERIAL DENSITY KGM LBIN
-ODULUS OF ELASTICITY -0A PSI
2EFERENCE DATA
#ALCULATION DATA
.OTE 4HE CYLINDER RUNNING CLEARANCE IS THE BORE )$
MINUS THE /$ ACROSS THE RIDER RINGS 5SE ACTUAL VALUES
FOR FINAL CALCULATIONS
Figure C-6A—Data for Rod Runout Calculation
Note: The cylinder running clearance is the bore ID minus the OD across the rider rings. Use actual values for final calculations.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
122
API STANDARD 618
Piston length
Rod length B
CE
head
Rod length C
Length X
Dial
indicators
Packing case
Crosshead running
clearance
Inner face of crosshead nut
Rod length A
Cylinder running
clearance
(to top of ring)
Piston
Piston rod
Crosshead
Crosshead guide
Stroke
Cylinder
Rider rings
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Throw number
Stage
Cylinder bore diameter
Cylinder running clearance
Crosshead running clearance
Stroke
Rod diameter
Rod length A
Rod length B
Rod length C Indicator Position
Rod length X Indicator Position
Rod material
Material density, kg/m3 (lb/in3)
Modulus of elasticity, MPa (psi)
1
1
20 in.
0.080 in., 0.060 in., 0.040 in., 0.020 in., 0.010 in.
0.020 in.
11 in.
3 in.
110 in.
95 in.
80 in.
14 in.
AISI 4140
0.283 lb/in.3
30 x 106 psi
Reference Data
Calculation Data
Notes: The cylinder running clearance is the bore ID
minus the OD across the rider rings. Use actual values
for final calculations.
This example is based on US customary units.
Figure C-6B—Rod Runout Calculation Example
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
123
C.5.4 For correct vertical rod runout calculations, it is important to use actual measured running clearances for the cylinder and
crosshead, as well as the actual measured dimensions of the dial indicator locations along the top of the piston rod. Correct rod
lengths as required by Figure C-6A are also important.
C.5.5 Rod runout should always be measured starting with the rod at the extreme end of the stroke, with the piston at the crank
end of the cylinder. The dial indicators should be zeroed. Manual bar-over should be such that the connecting rod runs over (that
is, over the top on the outstroke) as the crosshead, piston rod, and piston are stroked slowly outward toward the end of the stroke
at the head end of the cylinder. Dial indicator readings are observed during the stroke and recorded at the end of the stroke. If this
method, and the dial indicator positions noted in C.5.3 are used as the standard measurement procedure, then field runout readings
can be properly compared and evaluated with factory runout readings provided in Figure C-3.
C.5.6 The dimensions shown in Figure C-1, Figure C-2, Figure C-5, and used in Figure C-6B for the calculation example, were
selected for convenience in illustrating basic runout geometry and principles. Dimensions for actual compressors may vary
greatly from the illustration dimensions, while some may be close or identical. Since vertical rod runout will vary according to
stroke, rod length, rod sag, and the difference in running clearances between the crosshead and cylinder, different compressors
with different cylinder configurations may have significantly different vertical runout readings for conditions of perfect
alignment.
C.5.7 Excessive rod runout is corrected by realignment and/or squaring up some or all components involved. These may
include cylinders, liners, heads, distance pieces, crossheads and crosshead guides, and rods and pistons. Crosshead threads and
face, piston rod nut threads and face, and piston rod threads may have to be checked and corrected for perpendicularity. As a
check for squareness at the interface of the crosshead and piston rod, both horizontal and vertical runout should be checked first
with the crosshead nut loose and then tight. Certain conditions of excessive rod runout at the packing case can further be
evaluated by placing an dial indicator on the rod in the cylinder through a crank end valve port to verify full length liner
concentricity with the cylinder bore and/or cylinder crank end face squareness with the bore. With a dial indicator in the cylinder,
full stroke runout cannot be taken since the dial indicator takes up some of the space between the crank-end head and the piston.
However, the available stroke is sufficient to get a suitable reading to determine alignment status
C.6 Horizontal Runout
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Horizontal runout readings can be used as a direct indication of the horizontal alignment from the crosshead through the distance
pieces to the cylinder. No calculations are necessary, as horizontal runout should be within the zero limits regardless of whether
the unit is cold or hot, or of the axial location of the dial indicator along the side of the rod. It is measured by placing dial
indicators on the side of the rod as close as possible to the crosshead and the pressure packing case at the locations noted in C.5.2,
and shown in Figure C-6A. For perfect alignment, the dial indicators should read zero as the rod is moved slowly through the
entire length of the stroke during manual bar-over. The best indication of perfect horizontal alignment is when horizontal rod
runout measures zero with dial indicators set at both the crosshead end and the piston end of the rod, in other words, as close to the
packing case as possible. See 6.1.28 for allowable limit.
C.7 Vertical Runout
C.7.1 COLD RUNOUT
Cold vertical runout readings other than zero are not necessarily an indication of misalignment. When all components are
perfectly aligned, the normal cold vertical rod runout is the result of the difference between the cold running clearance of the
piston in the bore and that of the crosshead in the crosshead guide, plus the effect of normal rod sag, the length of the stroke, the
length of the rod, and the location of the dial indicators along the top of the rod. It is, therefore, important that the actual running
clearances for the cylinder and crosshead are used for the calculations, as well as the rod lengths and actual dial indicator locations
shown in Figure C-6A.
C.7.2 BASIC GEOMETRY
The basic geometry is illustrated in Figures C-1 and C-2. Piston and crosshead centerlines lie below the perfect alignment
centerline by one half of the running clearances. In cylinders where the running clearance is greater (or less) than the crosshead
running clearance, the piston will lie below (or above) the crosshead centerline by one half of the difference in the cold running
clearances. The result is basic vertical rod runout that is normally something other than zero for perfect alignment. This one-half
124
API STANDARD 618
clearance difference is referred to as the differential drop (U DROP). The basic geometry closely approximates a right triangle
condition.
Basic ideal vertical runout through the stroke length, as shown in Figure C-2, is determined by the normal running clearances and
resulting U DROP, the rod length, and the stroke. Assuming an ideal straight-rod situation, in other words, without sag, basic cold
vertical runout for perfect alignment can be calculated with sufficient accuracy using proportional right-triangle equations as
shown in Figure C-2, when these values are known. The principle can also be used to calculate U DROP at any point on the rod,
which is necessary to calculate vertical rod runout at specific dial indicator locations when combining U DROP with rod sag as
shown in Figures C-4 and C-5.
C.7.3 ROD SAG
Since all horizontal rods sag, especially those used in Types B, C, and D distance pieces, it is necessary to incorporate the effects
of deflection based on rod length, rod diameter, rod weight, and rod material into the vertical runout calculations. When vertical
rod runout readings are taken at several positions along the entire length of the piston rod, the readings will generally indicate that
sag for a long rod attached to a crosshead and to a piston, when installed in a compressor assembly with precise geometric parts
that have been proven to be perfectly aligned, will exhibit deflection characteristics similar to that for one end supported (at the
crosshead), and one end fixed (at the piston). For these reasons, it is necessary to calculate the expected vertical rod runout at the
crosshead end, and at the piston end of the rod based on Figure C-6A. Note that the data includes both dial indicator positions
along the top of the rod. The combined U DROP and deflection must be calculated at these dial indicator positions as shown in
Figures C-4 and C-5.
As can be seen from Figures C-4 and C-5, rod sag will cause different vertical runout readings at different dial indicator positions
along the top of the rod. For conditions of perfect alignment, at the lowest point of sag, runout readings may be nearly zero
depending on cylinder clearance (U DROP), while at the crosshead end, readings should always be positive. Next to the cylinder
packing case, readings may be positive, or they may be negative, depending on rod length, sag, and cylinder running clearance
(U DROP). The zero vertical runout position can usually be found by placing the dial indicator along the top of the rod until the
lowest point of sag is reached.
When the rod is stroked forward (that is, out toward the head end as noted in C.5.3 and shown in Figures C-4 and C-5), the dial
indicator at the crosshead should normally read positive.
C.8 Hot Runout
For large cylinders with aluminum pistons and Fluorocarbon wear bands, there can be a significant difference between the cold
rod runout and the hot runout. This is because of the high thermal expansion rate of the aluminum piston and the fluorocarbon
wear bands, which can result in a significant difference in the differential clearance between the piston and the crosshead. On the
other hand, there may be operating conditions involving low suction temperatures such that normal operating temperatures may
be no greater than the ambient temperature on which the cold vertical runout readings are taken. Expected hot runout can be
determined by calculating the expected thermal growth of the cylinders, the pistons, and the rider ring radial thickness. The
cylinder running clearance, affecting hot U DROP, is then adjusted accordingly in the vertical runout calculations.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Design and construction shall be aimed to achieve zero hot vertical rod runout at the packing case. Due to the effects of rod sag,
this may not always be attainable under conditions of perfect alignment; and it is necessary to determine whether the value should
be positive or negative. This can be seen from a study of Figure C-5C and the five curves illustrated by Figures C-7 through C-11.
Sometimes this requirement can be attained by shim adjustment of the crosshead shoes (see C.9), but a thorough study of cold
readings compared to expected results from computer calculations is required to determine what adjustments, if any, are needed,
or should be done to obtain the ideal desired vertical runout at operating temperatures. In many cases, where there is considerable
sag, it may be better to operate as is than attempt to adjust the vertical runout, particularly if the cylinder and crosshead guide
alignments are near perfect.
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
125
ROD RUNOUT
EXAMPLE OF COMPUTERIZED PRINTOUT USING THE CYLINDER DATA OF FIGURE C-5B
U.S. customary units
Piston rod runout calculation
By: Engineering
Piston rod runout calculation data
Throw number
Stage
Cylinder bore diameter
Cylinder running clearance
Crosshead running clearance
Stroke
Total rod length A
1
1
20.00
0.080
0.020
11
110
Standard calculated rod runout per Figure C-2
Vert rod runout - basis no sag
Hor rod runout
0.0030
0
Rod sag calculation data
rod diameter
rod length B
material density lb/in3
modulus of elasticity E
3
95
0.2830
3.00e+07
Moment of inertia I
Total rod weight
3.9761
190.0
Maximum deflection piston end fixed per
Figure C-3
Rod runout at cylinder
Rod runout at crosshead
Horz runout
0.007398
Calculated Runout
0.0008
0.0061
0
Ref: Runout sample
Customer: Runout
Size unit: 11 in. stroke
Ref: rod runout
At crosshead At cylinder
0.0061
0.0008
Ref: piston $ DROP = 0.030
Enter rod lengths as integers only
Limits
0.0047
0.0014
0.0017 -0.0017
Rod material
AISI 4140
Max at D = 0.4215 x length =
40.04 in. from free end (crosshead)
Ref: nominal runout due to sag = 0.0026
Runout Limits
0.0025
-0.0008
0.0077
0.0044
0.0017
-0.0017
ROD RUNOUT AT DIFFERENT CYLINDER CLEARANCES
Cylinder Running
Clearance (in.)
Crosshead Running
Clearance (in.)
$ DROP
Rod Runout (in.)
At Cylinder
At Crosshead
0.080
0.020
0.030
0.0061
+0.0008
0.060
0.020
0.020
0.0051
-0.0002
0.040
0.020
0.010
0.0041
-0.0012
0.020
0.020
0.000
0.0031
-0.0022
0.010
0.020
-0.005
0.0026
-0.0027
Note: See Figures C-6 through C-10
Figure C-6C—Sample Printout for Rod Runout
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
126
API STANDARD 618
Crosshead centerline
Face of crosshead
VERTICAL ROD RUNOUT
0
0.002
0.004
Rod
sag
0.006
DEFLECTION / RUNOUT
0.008
0.010
0.012
0.020 in. Crosshead
clearance
0.014
0.016
Pis
ton
0.018
0.020
0.080 in. Cylinder
clearance
rod
0.022
B
0.024
0.026
0.028
C
X
0.030
A
0.032
0
11
22
14 in.
Dial indicator
at crosshead
Runout 0.0061 in.
at crosshead
33
44
55
ROD LENGTH
66
77
88
99
80 in.
95 in.
Dial
CE face
indicator of piston
at cylinder
Runout 0.0008 in.
at cylinder
$ DROP 0.030 in.
110
HE face
of piston
REF: FIG C-5C
Figure C-7—Graphical Illustration of Rod Runout at 0.080 in. Cylinder Running Clearance
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
Ro
d
sa
g
VERTICAL ROD RUNOUT
0.020 in. Crosshead
clearance
0.060 in. Cylinder
clearance
Same as removing
0.010 in. shims from
bottom shoe of
crosshead relative to
Fig. C-6. Changes
rod runout by 0.001 in.
d
ro
0
0.001
0.002
0.003
0.004
0.005
0.006
0.007
0.008
0.009
0.010
0.011
0.012
0.013
0.014
0.015
0.016
0.017
0.018
0.019
0.020
0.021
on
st
Pi
DEFLECTION / RUNOUT
Crosshead centerline
Face of crosshead
127
B
C
X
A
0
11
22
14 in.
Dial
indicator
at crosshead
Runout + 0.0051 in.
at crosshead
33
44
55
ROD LENGTH
66
77
88
99
80 in.
95 in.
Dial
CE face
indicator of piston
at cylinder
Runout = –0.0002 in.
at cylinder
$ DROP 0.020 in.
110
HE face
of piston
REF: FIG C-5C
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Figure C-8—Graphical Illustration of Rod Runout at 0.060 in. Cylinder Running Clearance
128
API STANDARD 618
Crosshead centerline
Face of crosshead
VERTICAL ROD RUNOUT
0
–0.001
ag
–0.002
0.020 in. Crosshead
clearance
–0.004
–0.005
0.040 in. Cylinder
clearance
–0.006
Same as removing
0.020 in. shims from
bottom shoe of
crosshead relative to
Fig. C-6. Changes
rod runout by 0.002 in.
–0.007
to
Pis
od
nr
–0.008
–0.009
B
$ DROP 0.010 in.
–0.010
–0.011
B
X
X
A
–0.012
0
11
22
33
14 in.
Dial
indicator
at crosshead
Runout = + 0.0041 in.
at crosshead
44
55
ROD LENGTH
66
77
88
99
110
80 in.
95 in.
Dial
CE face
indicator of piston
at cylinder
HE face
of piston
Runout = –0.0012 in.
at cylinder
REF: FIG C-5C
Figure C-9—Graphical Illustration of Rod Runout at 0.040 in. Cylinder Running Clearance
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
DEFLECTION / RUNOUT
Ro
ds
–0.003
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
Crosshead centerline
Face of crosshead
VERTICAL ROD RUNOUT
$ DROP 0.0 in.
Crosshead and
piston on same
centerline
0
–0.001
0.020 in. Crosshead
clearance
–0.003
0.020 in. Cylinder
clearance
d=
Rod
sag
–0.002
n ro
–0.004
–0.005
Same as removing
0.030 in. of shims from
bottom shoe of
crosshead relative to
Fig. C-6. Changes
rod runout by 0.003 in.
Pist
o
DEFELCTION / RUNOUT
129
–0.006
–0.007
C
X
B
A
–0.008
0
11
22
33
14 in.
Dial
indicator
at crosshead
Runout = + 0.0031 in.
at crosshead
44
55
ROD LENGTH
66
77
88
99
80 in.
95 in.
Dial
CE face
indicator of piston
at cylinder
Runout = – 0.0022 in.
at cylinder
110
HE face
of piston
REF: FIG C-5C
Figure C-10—Graphical Illustration of Rod Runout at 0.020 in. Cylinder Running Clearance
--``,,,``,,`````,``,,,
130
API STANDARD 618
Crosshead centerline
VERTICAL ROD RUNOUT
Face of crosshead
–0.006
$ DROP –0.005 in.
–0.005
–0.004
–0.003
0.020 in. Crosshead
clearance
–0.001
0.010 in. Cylinder
clearance
0.000
0.001
Ro
ro
d
0.003
ds
ag
0.002
Less cylinder
clearance than
crosshead clearance
Pis
to
n
DEFLECTION / RUNOUT
–0.002
0.004
0.006
0.008
A
B
0.007
X
0
11
C
22
14 in.
Dial
indicator
at crosshead
Runout + 0.0026 in.
at crosshead
33
44
55
ROD LENGTH
66
77
88
99
80 in.
95 in.
Dial
CE face
indicator of piston
at cylinder
110
HE face
of piston
Runout = –0.0027 in.
at cylinder
Figure C-11—Graphical Illustration of Rod Runout at 0.010 in. Cylinder Running Clearance
C.9 Vertical Runout Adjustment
C.9.1 If it is believed that some adjustment is necessary to the vertical runout readings, it must first be assured that cylinder
alignment and cylinder level are properly set so that the components are free of harmful stresses at operating conditions. If
crosshead shim adjustment is then considered necessary by interchanging shims under the crosshead shoes, it should be
remembered that taking shims from the bottom shoe and placing them under the top shoe drops the crosshead centerline further
below the perfect alignment centerline. This decreases the U DROP and thus decreases the positive rod runout at the crosshead,
but may actually increase negative runout at the packing case due to sag. This is illustrated on Figure C-5C and in the series of
five runout curves of Figures C-6 through C-10.
With reference to Figures C-6 and C-9, note that a 0.76 mm (0.030 in.) change of shims, that would put the crosshead and piston
on the same centerline such that U DROP = 0.00, changes the runout by only 0.076 mm (0.003 in.), that is, the crosshead runout
goes to +0.079 mm (+0.0031 in.) from +0.155 mm (+0.0061 in.), and the runout at the packing case goes to –0.056 mm (–0.0022
in.) from +0.020 mm (+0.0008 in.). In other words, for this example, rod runout is changed by only 0.0254 mm (0.001 in.) for
each 0.254 mm (0.010 in.) of shims removed from the bottom shoe in an attempt to lower the crosshead closer to the centerline of
the cylinder. Because rod length and rod diameter, which affect sag, and cylinder size, which affects running clearance, can
significantly affect vertical runout, every compressor cylinder assembly must be fully evaluated for expected vertical runout
based on perfect alignment conditions. If crosshead shims are shifted in an attempt to adjust vertical runout, it is important that the
crosshead always be installed with the “top” side up following removal for maintenance.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
0.005
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
131
These illustrations also demonstrate the importance of using the actual measured running clearances of the cylinder and crosshead
when calculating and evaluating vertical rod runout since a change of cylinder running clearance will affect U DROP which in
turn affects vertical runout. For some combinations of cylinder size, rod length, and stroke, the cylinder clearance will have a
greater effect on vertical rod runout than other combinations. As illustrated in Figures C-1 and C-2, it can be seen that the longer
the stroke, the greater the runout; and the shorter the piston rod, the greater the runout, for the same U DROP.
To see the effect of rider ring wear on vertical rod runout, use Figure C-10 as the initial reference and compare it to Figure C-9,
which has a U DROP of 0.254 mm (0.010 in.). The 0.254 mm (0.010 in.) drop is representative of 0.254 mm (0.010 in.) rider ring
wear, which changes the vertical rod runout by 0.0254 mm (0.001 in.) to 0.030 mm (0.0012 in.) from 0.056 mm (0.0022 in.).
Where there is much concern about rod runout, each application needs to be studied carefully in order to fully understand what the
vertical rod runout should be under conditions of perfect alignment in order to make the right decision and proper adjustment.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
C.9.2 If crosshead shim adjustment has been considered necessary by interchanging shims under the crosshead shoes, the final
arrangement shall be recorded in the as-built data sheet included in the operation and maintenance manual.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex D
(informative)
Repairs to Gray or Nodular Iron Castings
D.1 Scope
This annex covers repair procedures that have been successfully applied to gray and nodular iron castings for compressor
cylinders and related parts in various services. These procedures are only briefly described for the purpose of reference by the
purchaser and the vendor; detailed descriptions of the procedures are beyond the scope of this standard. Limitations on the use of
the procedures are included. These procedures should be applied only after careful evaluation of the situation by the purchaser
and the vendor. When the service conditions of the casting involve toxic or hazardous gases, an even more exhaustive evaluation
should be made.
D.2 Repair methods and limitations
In cylinders designed to handle gases having a mean molar mass (molecular weight) below 12, no repairs of any type shall be
made to defects that result in leakage between the cylinder bore and the water jacket during hydrostatic testing. With the
purchaser’s written approval, the repair methods specified in D.2.1 through D.2.3 may be used for compressor cylinders designed
to compress gases with a mean molar mass of 12 or greater.
D.2.1 Areas in which hydrostatic testing shows leaks between the water jacket and the atmosphere or between the gas passage
and the atmosphere or between the water jacket and the gas passage may be repaired by plugging per 6.13.6.5.2, or by approved
procedures for vacuum-plus-pressure impregnating. Impregnating may be considered only for limited porosity-type leakage and
only after hydrostatic testing of both the water jacket and the gas passage has proved the mechanical integrity of the casting.
D.2.2 Defects that show up on machined surfaces or in other areas where no leak is involved, may be repaired by iron plating.
Such defects could include porosity in valve seats or head and cylinder end faces or out-of-tolerance of cylinder bores requiring a
liner. Plating repairs are not acceptable in critical areas such as o-ring seating areas or surfaces swept by the compressor piston,
where sharp edges could damage o-rings, piston rings, and so forth. If repair plating is used in other locations, no sharp corners
shall be formed or left which could damage o-rings, etc. (see 6.13.6.5).
D.2.3 Damaged threaded holes in castings may be mechanically repaired by use of thread inserts or bushings.
D.3 Tests
After any part is repaired in accordance with D.2.1, D.2.2, or D.2.3, the part shall be subjected to both a hydrostatic test and a gas
test (see 8.3.2).
133
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--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex E
(informative)
Purchaser’s Checklist
This checklist may be used to indicate the purchaser’s specific requirements when this standard indicates, with a bullet (•), that a
decision or information is required from the purchaser.
The checklist should be used in conjunction with the data sheets (Annex A). Below, the purchaser should circle yes or no, or mark
the appropriate space with an “X”, or fill in the requirements.
Note: The use of this checklist is optional where these Items are covered by a narrative specification.
Clause
2.3
5.1
6.1.3
6.1.5
6.1.6
6.1.12
6.1.17
6.1.20
6.1.21
6.1.22
6.4
6.5.2
6.8.2.4
6.8.3.5.2
6.8.4.1.16
6.8.4.1.17
6.12.1.1
6.9.1.9
6.9.2.1
6.10.3.2
6.11.5
6.12.1.1
6.12.1.4/5
6.12.2.1
6.12.2.3
6.12.2.4c
6.13.1.1
6.13.2.7
6.13.1.6
6.14.2.1.3
6.14.2.2
6.14.2.5
6.14.2.6
6.14.2.1.10
Question
Answer
Applicable standards:_________________________________________________________________________________
Have units of measurement been specified?
Yes
No
Has equipment’s normal operating point been specified?
Yes
No
Has the pressure design code been specified?
Yes
No
Requirements and maximum allowable sound pressure level?
Requirement:________________________________________________________________________________________
Maximum allowable sound pressure level: ______________dB (A)
Area classification for electrical components?
Applicable standards:_________________________________________________
Are local codes and regulations applicable?
Yes
No
Which details of an initial installation check shall be agreed by vendor and
purchaser?_____________________________________________________________________
Yes
No
Operating temperature alignment check?
Location and environmental conditions (see data sheet, page 2).
Have utility streams been identified?
Yes
No
Equipment’s normal operating point specified in the data sheet, page 1?
Yes
No
Values specified by the purchaser, based on his experience?
for: maximum average piston speed: ____________________ m/s
for: maximum speed: ________________________________ rpm
Is 100% unloading necessary?
Yes
No
Is coating of the running bore of the cylinder required?
Yes
No
Self-contained, forced circulation, closed jacket cooling system to be furnished by the vendor:
Yes
No
DN 12 indicator tap at each end of each cylinder?
Yes
No
Have indicator valves been specified?
Yes
No
Type of distance piece, specified in data sheet, page 8?
Yes
No
Shall the vendor submit a written valve dynamics report?
Yes
No
Is unloading to be specified (data sheet, page 3)?
Yes
No
Purchaser requires wear bands?
Yes
No
Are relief devices for crankcases required?
Yes
No
Has type of distance piece been specified (data sheet, page 8)?
Yes
No
Provision for intermediate packing sealing gas required?
Yes
No
Type of distance piece covers required:
Mesh screens / Louvered Solid metal / Other
Is higher partition differential pressure specified?
Yes
No
Is distance piece purge or vacuum connection specified?
Yes
No
Are shields in the crosshead housing over the oil return drains required?
Yes
No
Closed liquid cooling system for packing to be supplied?
Yes
No
Venting and buffer gas cups for cylinder pressure packing required?
Yes
No
Is special purpose oil system specified?
Yes
No
Has the type of driver for auxiliary lube oil pump been specified on the data sheet, page 11?
Yes
No
Has the heating device for oil reservoir been specified on the data sheet, page 5?
Yes
No
Shall the relief valve for crankcase driven pump be mounted outside the crankcase?
Yes
No
Shall oil system be run in vendors shop?
Yes
No
135
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Table E-1—Purchaser’s Checklist
136
API STANDARD 618
Table E-1—Purchaser’s Checklist (Continued)
Clause
6.14.3.1.1
6.14.3.1.2
6.14.3.1.4
6.14.3.1.6
6.14.3.1.9
6.14.3.2.2
6.15.1.5
6.15.1.8
6.15.1.11
6.15.5.12
6.15.5.13
6.15.6.5
6.15.7.5
6.15.7.6
6.15.8.1
6.16.7
7.1.1.1
7.1.1.5
7.1.1.6
7.1.2.1
7.1.2.3
7.1.2.4
7.1.2.15
7.1.3.1
7.1.3.2
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
7.2.1.3
7.2.1.7
7.2.2.1
7.3.1
7.5.1.1
7.5.3.5
7.5.3.9
7.5.4.1
7.5.4.8
7.5.4.9
7.5.4.14
7.5.4.15
7.5.5.1
7.5.5.4
7.6.1.2
7.6.2.1
7.6.2.2
Question
Answer
Has the type of lubricator for compressor cylinders and for the pressure packing lubrication been
Yes
No
specified on the data sheet, page 9?
How shall lubricator to be driven?
From crankshaft / Independently
Is a heating device with thermostatic control for the lubricator reservoir required?
Yes
No
Which alarm functions for cylinder and pressure packing lubrication are required?
for cylinder:______________________________________________________________________________
for pressure packing:_______________________________________________________________________
(See data sheet, page 16)
Are synthetic lubricants of compressor cylinder lubrication required and specified in data sheet,
Yes
No
page 9?
Is an agreement for additional or alternative protection device for divider block lubrication
Yes
No
required?
Are additional material tests specified?
Yes
No
Has the presence and maximum amounts of corrosive, reactive or hazardous agents or
Yes
No
components in the process fluid been specified on the data sheet, page 2?
Has the amount of hydrogen sulfide been specified on the data sheet, page 2?
Yes
No
Is additional inspection required for specific welds?
Yes
No
Shall the proposed welding designs of fabricated cylinders be available for purchaser’s review?
Yes
No
Shall purchaser be given notice of repairs to major components?
Yes
No
Is 100 % radiography of butt welds or magnetic particle inspection or liquid inspection of welds
Yes
No
required?
Shall proposed connection sketches be submitted to the purchaser before fabrication?
Yes
No
Has the minimum design metal temperature related to the expected operating conditions been
Yes
No
specified?
Shall US customary or SI units be shown on the nameplates?
US customary units / SI units
Has the type of driver been specified on the data sheet, page 1?
Yes
No
Are there process-variations or start-up conditions that affect driver selection?
Yes
No
Are the driver starting conditions specified on the data sheet?
Yes
No
Have the type of motor, its characteristics and accessories been specified on the data sheets?
Yes
No
Shall single bearing motors be provided with a temporary inboard support device?
Yes
No
Has the reduced voltage for starting-torque requirements been specified?
Yes
No
Shall hydrodynamic motor bearings be supplied with oil from compressor frame lubrication
Yes
No
system (data sheet, page 5)?
Has the standard for turbine drivers been specified?
Yes
No
Is a separate lube oil system for turbine drive train in accordance with ISO 10 438 (or API Std
Yes
No
614) required?
Are couplings required to comply with API Std 671 (data sheet, page 4)?
Yes
No
Are couplings for auxiliary drives required to comply with API Std 671 (data sheet, page 4)?
Yes
No
Has the standard for guards been specified on data sheet, page 4?
Yes
No
Has the standard for gear units been specified on data sheet, page 4?
Yes
No
Has the type of mounting plates been specified on the data sheet, page 4?
Yes
No
Have chock blocks been specified on the data sheet, page 4?
Yes
No
Have leveling plates been specified on data sheet, page 4?
Yes
No
Has the major equipment to be mounted on a baseplate been indicated on the data sheet, page 4?
Yes
No
Has a baseplate suitable for column mounting been specified on the data sheet, page 4?
Yes
No
Shall the baseplate be designed to facilitate optical, laser, or other accurate leveling in the field?
Yes
No
Shall a dynamic response analysis of the skid be performed?
Yes
No
Shall sub-soleplates be provided with the baseplate?
Yes
No
Have soleplates or rails been specified on the data sheet, page 4?
Yes
No
Shall sub-soleplates be supplied for soleplates?
Yes
No
Are all auxiliary system instrumentation be provided by the vendor specified?
Yes
No
Which sensing lines handling hazardous fluids require transduced
signals?____________________________________________________________________________________________
Source of the control signal and its sensitivity and range?_____________________________________________________
Has the configuration of the control system been specified?
Yes
No
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
137
Table E-1—Purchaser’s Checklist (Continued)
Clause
7.6.2.4
7.6.4.1
7.6.4.2
7.6.4.3.3
7.6.4.3.4
7.6.6.4
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Question
Answer
Is an automatic loading-delay interlock required?
Yes
No
Have instruments for local, gauge board, or instrument panel been specified?
Yes
No
Has a tachometer to indicate compressor speed been specified on the data sheet, page 17?
Yes
No
Have temperature detectors for packing been specified on the data sheet, page 16?
Yes
No
Have temperature detectors for main bearings and valves been specified on data sheet, page 16?
Yes
No
Has the extent of the alarm/shutdown system to be supplied by the vendor been specified on data
Yes
No
sheet, page 16?
7.6.6.6
Has the design of alarm and shutdown circuits been specified?
Yes
No
7.6.6.7
Have high temperature alarms for crosshead pins been specified on data sheet, page 16?
Yes
No
7.6.7.1
Shall the vendor furnish and mount vibration detection and transducing devices?
Yes
No
7.6.7.2
Shall a non-contacting proximity device to measure vertical movement of each piston rod be
Yes
No
installed?
7.6.7.3
Shall a one-event-per-revolution mark be provided on the crankshaft?
Yes
No
7.6.7.4
Shall the vendor provide piston rod drop detectors?
Yes
No
7.6.8
Shall the vendor supply a temperature monitoring system in accordance with API Std 670?
Yes
No
7.7.1.2
Has the extent of piping system to be supplied by the vendor been specified on data sheet, page 4?
Yes
No
7.7.1.4
Shall piping, pulsation suppression devices and knockout vessels be arranged for heat tracing and
Yes
No
insulation (see 7.9.5.1.17)?
7.7.1.6
Shall the vendor review the drawings of all upstream and downstream piping, appurtenances,
Yes
No
vessels and supports?
7.7.1.13
Special requirements for piping, flanges, valves and other appurtenances for hydrogen, hydrogen sulphide or toxic
services?____________________________________________________________________________________________
7.7.2.5
Is a continuous through flow for instrument sensing lines to safety switches required?
Yes
No
7.7.4.3
Shall coolant piping on the compressor be furnished by the vendor?
Yes
No
7.7.6.1
Extent of process piping to be furnished by the
vendor?____________________________________________________________________________________________
7.7.6.3
Have design, location, and orientation of start-up screens been agreed?
Yes
No
7.7.6.4
Shall a removable spool piece for start-up screens be supplied?
Yes
No
7.8.1.1
Has the type of intercoolers to be furnished by the vendor been specified?
Yes
No
7.8.1.2
Has the type of aftercoolers to be furnished by the vendor been specified?
Yes
No
7.8.2.1
Shall liquid separation and collection facilities be provided?
Yes
No
7.8.2.7
Shall an automatic drainage system be provided?
Yes
No
7.8.2.8
Shall level indicator and alarm and shutdown devices be provided?
Yes
No
Has piping between compressor stages and the intercoolers and aftercoolers furnished by the
Yes
No
vendor been specified on data sheet, page 4?
7.9.2
Have alternate gases, conditions of service, or start-up been specified?
Yes
No
7.9.3.1
Will compressor be operated in conjunction with other compressor units (data sheet, page 4)?
Yes
No
7.9.3.2
Has Design Approach 1 been specified (data sheet, page 4)?
Yes
No
7.9.4.1.2
Shall the analysis be performed by the vendor or a third party?
Vendor / Third party
7.9.4.2.5.2.2.4 Has criteria for flow pulsations in systems with sensitive elements been agreed upon?
Yes
No
7.9.4.2.5.2.5.2 Shall a piping system flexibility analysis be performed?
Yes
No
7.9.5.11
Shall the pulsation suppressors be stamped with the symbol of the specified pressure vessel code?
Yes
No
7.9.5.1.4
Shall butt welds of pulsation suppression devices be 100% radiographed?
Yes
No
7.9.5.1.7
Shall a final moisture removal section be included in the suction suppression device?
Yes
No
7.9.5.1.10 Has purchaser approved use of circular notched baffles?
Yes
No
7.9.5.1.11 Shall a thermowell connection for the cylinder nozzle of each suction pulsation suppressor be
Yes
No
provided?
7.9.5.1.17 Has provision for insulation at pulsation suppression devices been specified on the data sheet,
Yes
No
page 14?
7.9.5.1.20 Shall internals of carbon steel suppressors be coated with phenolic or vinyl resin?
Yes
No
7.9.5.1.22 Shall dynamic and static stresses from pulsation-induced forces be analyzed?
Yes
No
7.9.6
Shall the vendor supply supports for the pulsation suppression devices and for vendor supplied
Yes
No
piping?
7.10.1
Has purchaser specified special design details for air intake filters?
Yes
No
7.11.2
Shall hydraulic tensioning tools be included in special tools?
Yes
No
138
API STANDARD 618
Table E-1—Purchaser’s Checklist (Continued)
8.2.1.1 f
8.2.1.3
8.2.2.1.1
8.2.3.2
8.2.3.3
8.2.3.4
8.3.3.2
8.3.3.3
8.3.3.6
8.3.3.7
8.3.4.2
8.3.4.4
8.4.1
8.4.14
9.2.3m
9.2.3s
9.3.1.3
9.3.3.1
9.3.3.3
9.3.3.4
Question
Answer
Shall the compressor be fitted with a device to lock the shaft in position during maintenance?
Yes
No
Is purchaser’s inspector to submit completed inspection checklist before shipment?
Yes
No
Has the extent of purchaser’s participation in the inspection and testing and amount of advance
Yes
No
notification been specified on the data sheet, page 9?
Shall the vendor keep available for at least 20 years final-assembly, maintenance and running
Yes
No
clearances?
Which parts shall be subjected to surface and subsurface
examination?:________________________________________________________________________________________
and which type of examination is required?: ________________________________________________________________
Required radiographic, ultrasonic, magnetic particle or liquid penetrant inspection of welds or
materials?
— radiographic
Yes
No
Yes
No
— ultrasonic
Yes
No
— magnetic particle
Yes
No
— liquid penetrant
Shall the oil system be run in the manufacturer’s shop?
Yes
No
Has inspection for cleanliness of the equipment and all piping and appurtenances by the purchaser
Yes
No
been specified on the data sheet, page 9?
Shall the hardness of parts, welds and heat-affected zones be tested?
Yes
No
Has a 4-hour running test of the compressor been specified on the data sheet, page 9?
Yes
No
Is a 4-hour mechanical running test prior to shipment required for packaged units, including
Yes
No
auxiliary system packages?
Is an operational test and a 4-hour mechanical running test prior to shipment for auxiliary system
Yes
No
consoles required?
Is dismantling for inspection required?
Yes
No
Shall all machine-mounted equipment, prefabricated piping and appurtenances furnished by the
Yes
No
vendor be fitted and assembled in the vendor’s shop?
Shall the compressor be performance tested in accordance with ISO 1217?
Yes
No
Time for storage for a longer period than 6 months?__________________________________________________________
Shall the equipment be packed for domestic or export shipment?
Domestic / Export
Special requirements for long term storage of spare parts?_____________________________________________________
Is a list of similarly installed machines to be attached to the proposal required?
Yes
No
Has time allowed for the purchaser to review vendor’s data been specified and agreed? (see
Yes
No
VDDR form in Annex F)
Shall the vendor submit performance curves or tables etc.?
Yes
No
Shall the vendor furnish data required for independent rod-load, gas-load and rod-load reversal
Yes
No
calculations?
Shall the effect of valve failure on rod loads and reversals be calculated and furnished?
Yes
No
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Clause
7.11.5
8.1.2
8.1.6
Annex F
(normative)
Vendor Drawing and Data Requirements
F.1 General
This annex consists of a sample vendor drawing and data requirement form (VDDR), followed by a list of possible Items that may
be included on the form and representative descriptions of those Items. Since different manufacturers will use different names for
the same drawing, the Items in the description column of the VDDR should be modified in the early stages of the order using the
drawing names supplied by the manufacturer.
09
Insert VDDR form here (see Errata 1 at end of document).
F.2 Items for VDDR Form
Items to be entered on the VDDR should be selected from the following list as appropriate. However, this list is not necessarily
all-inclusive.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
1. Certified dimensional outline drawing (general arrangement) and list of connections.
2. Foundation plan showing anchor bolt locations.
3. Allowable flange loading (either cylinder or pulsation suppression device) and coordinates.
4. Driver outline.
5. Drive arrangement drawing.
6. Dimensional outline for all vendor-supplied major accessory equipment.
7. Performance data.
8. Pressure packing drawing(s).
9. Gas load, rod load, and crosshead load reversal and duration charts.
10. Starting torque versus speed curves (for driver and compressor.)
11. Motor driver performance characteristics.
12. Tabulation of utility requirements.
13. List of unsafe or undesirable speeds.
14. Gear data.
15. Other driver data.
16. Shaft coupling assembly drawing and bill of materials.
17. Weld procedures for fabrication and repair, including those for pulsation suppression devices.
18. Intercooler and aftercooler data.
19. Parts list with sectional drawings.
20. “Start-up” spares list.
21. Recommended normal maintenance spare parts.
22. Process schematic.
23. Frame and cylinder lube oil schematics and bills of materials.
24. Lube oil system assembly drawings and list of connections.
25. Lube oil system component drawings and data.
26. Cooling system schematics and bills of materials.
27. Cooling system assembly drawings and list of connections.
28. Cooling system component drawings and data.
29. Distance piece vent, drain and buffer schematics and list of connections.
30. Capacity control schematics and bill of materials.
31. Instrumentation and electrical schematics and bills of materials.
32. Instrumentation and electrical arrangement drawing and list of connections.
33. Instrumentation and electrical wiring diagrams.
34. Instrumentation set-point list.
35. Instrumentation data sheets.
36. Pulsation suppression device detail drawings and final pressure code calculations.
139
140
API STANDARD 618
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
37.
38.
39.
40.
41.
42.
43.
44.
45.
46.
47.
48.
49.
50.
51.
52.
53.
54.
55.
56.
57.
58.
59.
60.
61.
62.
63.
64.
65.
66.
67.
68.
69.
70.
71.
Special tools list.
Fabrication, testing and delivery schedule.
Drawing list.
Weather protection and climatization required.
Comments on purchaser’s piping and foundation drawings.
Progress reports.
Torsional analysis report.
Data for an independent torsional analysis.
Acoustic and mechanical analysis report.
Data required for third- party acoustic and mechanical analysis.
Engineering analysis for fabricated cylinders.
Balancing data tabulation.
Valve dynamics report.
Data for an independent valve dynamic analysis.
Connection sketches.
Shaft alignment diagram.
As-built dimensions and data.
Hydrostatic and gas test certificates.
Certified mechanical run test data (if test ordered).
Certified performance test data (if test ordered).
Non-destructive test procedures for fabricated cylinders.
Procedures for special or optional tests (if tests ordered).
Certified data from special or optional tests (if tests ordered).
Certified mill test reports.
Crankshaft ultrasonic test certificate.
Valve leak test certificate.
As-built data sheets.
Installation manual.
Operation and maintenance manual.
Technical data manual.
Procedures for preservation, packing and shipping.
Shipping list.
Material Safety Data Sheets.
Quality plan.
Control logic diagrams.
F.3 Description of VDDR Items
1. Certified dimensional outline drawings (general arrangement) and tables include, but are not limited to, the following:
a. Size, type, rating, location and identification of all customer connections; including vents, drains, lubricating oil, conduits,
conduit boxes, electrical and pneumatic junction boxes and instruments. The vendor’s plugged connections shall be identified.
Details of special connections are required. See 6.8.2.4.1.
b. The mass (weight) of each assembly, of the heaviest piece of equipment which must be handled for erection and of
significant Items to be handled for maintenance.
c. All principal dimensions, including those required for piping design, maintenance clearances and dismantling clearances,
Including valve maintenance clearance if pulsation suppression devices are not supplied.
d. Shaft center line height.
e. Shaft end separation.
f. Center of mass (gravity), vertical and plan location.
g. Direction of rotation.
h. When applicable, the make, size and type of couplings and the location of guards and their coverage.
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
141
2. Foundation plan including:
a. Dimensions of mounting plates for the complete train and auxiliary systems complete with diameter, number and location of
bolt holes and thickness of metal through which bolts must pass.
b. Speed, critical speed (if any),
c. Location and direction in the x, y, z-coordinate system of static and the first and second order dynamic (unbalanced) forces
and moments.
d. Location of the center of mass.
e. Leveling jackscrew location.
3. Allowable flange loading (either cylinder or pulsation suppression device) and coordinates (see 6.6.5). Allowable flange
loading(s) for all cylinder (or pulsation bottle) connections, including anticipated thermal movements referenced to a defined
point, and x, y, z-coordinate system.
4. Driver outline. Certified dimensional outline drawing for the driver and all its auxiliary equipment including:
a. Size, location, orientation and purpose of all customer connections, including conduit boxes, conduit, instrumentation and
any piping or ducting.
b. Type, rating and facing for any flanged connections.
c. Size and location of anchor bolt holes and leveling jackscrews and thickness of sections through which bolts must pass.
d. Total mass of each Item of equipment (driver and auxiliary equipment). plus loading diagrams, heaviest weight, and name of
the part.
e. Overall dimensions and all horizontal and vertical clearances necessary for dismantling and the approximate location of
lifting lugs.
f. Shaft center line height.
g. Shaft end dimensions, plus tolerances for the coupling.
h. Direction of rotation.
5. Drive arrangement drawing, including, but not limited to the following:
a. Flywheel data.
b. Driver and mechanical transmission mass.
c. Moments of inertia.
d. Stator shift.
e. Air gap.
6. Dimensional outline for all vendor supplied major accessory equipment.
7. Performance data (see 9.3.3.1).
8. Pressure packing drawing(s). (One for each packing type.)
9. Gas load, rod load and crosshead load reversal and duration charts (see 9.3.3.2).
10. Starting torque versus speed curves. (For driver and compressor—on the same chart.) Acceleration time (see 9.3.3.5).
11. Motor driver performance characteristics and performance data including:
a. For induction motors 150 kW (200 hp) and smaller:
1. Efficiency and power factors at one-half, three-quarter and full load.
2. Speed-torque curves.
b. For induction motors larger than 150 kW (200 hp), certified test reports for all tests run and performance curves as follows:
1. Time-current heating curve.
2. Speed-torque curves at 70%, 80%, 90% and 100% of rated voltage.
3. Efficiency and power factor curves from 0 to rated service factor.
4. Current versus load curves from 0% – rated service factor.
5. Current versus speed curves from 0% – 100% of rated speed.
6. Permissible safe stall time and repeated start capability (hot and cold).
c. For synchronous motors.
1. Speed-torque, current-speed and power factor-speed curves at 70%, 80%, 90% and 100% of rated voltage.
2. Pull-in and pull-out torque.
3. Permissible safe stall time and repeated start capability (hot and cold).
4. Efficiency and power factor curves from 0 to rated service factor.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
142
API STANDARD 618
5. Current pulsation-speed curve during normal acceleration.
12. Tabulation of utility requirements (may be on data sheets).
13. List of unsafe or undesirable speeds (see 6.1.10).
14. Gear Data.
a. Certified dimensional outline drawings and list of connections including:
1. The size, rating, location and identification of all customer connections including vents, drains, lube oil, conduit boxes,
junction boxes and instruments.
2. All principal dimensions, including those required for the purchaser’s foundation, piping design, maintenance clearances
and dismantling clearances.
3. Overall and handling masses.
4. Shaft center line heights.
5. Shaft end dimensions and tolerances for the couplings.
6. Direction of rotation.
7. Location of the center of mass of the gear unit.
8. The size and location of anchor bolt holes and thickness of sections through which bolts must pass.
9. Thermal and mechanical movements of casings and shafts.
b. Cross-sectional drawing and bill of materials including axial gear and pinion float.
c. As-built data sheets including:
1. Data for torsional analysis.
2. Lateral critical speed reports when specified.
3. Certified mechanical running test data.
d. Certified gear manufacturer’s standard test data including gear contact test data.
e. Optional test data and reports agreed upon by the purchaser and the gear manufacturer.
f. Spare parts recommendations.
15. Other driver data, including:
a. Cross-sectional drawing and bill of materials, including the axial rotor float.
b. As-built data sheets.
c. Certified drawings of driver auxiliary systems including wiring diagrams for each auxiliary system supplied. The drawings
shall clearly indicate the extent of the system to be supplied by the manufacturer and the extent to be supplied by others.
d. Spare parts recommendations.
e. Other driver data per driver VDDR.
16. Shaft coupling assembly drawing and bill of materials, including:
a. Allowable misalignment.
b. Hydraulic mounting procedure.
c. Shaft end gap and tolerance.
d. Coupling guards.
17. Weld procedures for fabrication and/or repair, including those for pulsation suppression devices (see 7.9.3.3).
18. Intercooler and aftercooler data, including, but not limited to:
a. Dimensional outline drawings.
b. Data sheets (e.g., TEMA).
c. Final calculation in accordance with the specified pressure code.
19. Parts list with sectional drawings. The parts list shall include pattern number, stock or production drawing numbers and the
materials of construction. The list shall completely identify each part so that the purchaser may determine interchangeability of
parts with other equipment furnished by the same manufacturer. Standard purchased Items shall be identified by the original
manufacturer’s name and part number. Materials shall be identified as specified in 6.15.1.2.
20. “Start-up” spares list (see 9.2.3i).
21. Recommended normal maintenance spare parts (see 9.3.6).
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
143
22. Process schematic:
Schematic diagram of the process fluids flowing through the machine, including:
a. Steady-state and transient gas flow rates, temperatures and pressures.
b. Cooler heat loads.
c. Pipe, tubing and valve sizes of equipment provided by the vendor.
d. Instrumentation, safety devices and control schemes.
e. Bill of materials.
23. Frame and cylinder lube oil schematics, including the following:
a. Steady-state and transient oil flows and pressures at each point.
b. Control, alarm and trip settings (pressure and recommended temperatures).
c. Total heat loads.
d. Utility requirements, including electrical, water and air.
e. Pipe, tubing and valve sizes.
f. Instrumentation, safety devices and control schemes.
g. Bills of materials.
24. Lube-oil system assembly drawings and list of connections.
Lube-oil system assembly and arrangement drawing(s), including size, rating and location of all customer connections.
25. Lube-oil system component drawings and data, including:
a. Outline and sectional drawings and data sheets for auxiliary pumps and drivers.
b. Outline and sectional drawings and data sheets for coolers, filters and reservoir.
c. Instrumentation.
d. Spare parts lists and recommendations.
26. Cooling system schematics and bill of materials.
Cooling (including packing cooling) or heating schematic and bill of materials including cooling or heating fluid, fluid flows,
pressure, pipe and valve sizes, instrumentation and orifice sizes.
27. Cooling system assembly drawings and list of connections.
Cooling (including packing cooling) or heating system assembly and arrangement drawing(s), including size, rating and location
of all customer connections.
28. Cooling system component drawings and data.
a. Outline and sectional drawings and data sheets for pumps and coolers.
b. Outline and sectional drawings and data sheets for coolers, filters and reservoir.
c. Instrumentation.
d. Spare parts lists and recommendations.
29. Distance piece vent, drain and buffer schematics and list of connections.
Distance piece vent, drain and purge schematic and bill of materials including fluid, fluid flows, pressure, pipe, tube and valve
sizes and instrumentation.
30. Capacity control schematics and bill of materials.
31. Instrumentation and electrical schematics and bills of materials for all systems, including pneumatic and hydraulic systems
(including bar over device limit switch).
32. Instrumentation and electrical arrangement drawing and list of connections, including pneumatic and hydraulic systems and
including but not limited to:
a. Control panel general arrangement.
b. Control panel certified outline.
c. Control panel bill of materials.
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144
API STANDARD 618
33. Instrumentation and electrical wiring diagrams for all systems.
34. Instrumentation set-point list, including set points for all alarm, shutdown and control devices, including:
a. Vibration alarm and shutdown limits.
b. Bearing temperature alarm and shutdown limits.
c. Lube oil temperature alarm and shutdown limits.
d. Lube oil pressure alarm and shutdown limits.
e. Gas discharge temperature alarm and shutdown limits.
f. Frame oil level alarm limit.
g. Rod packing temperature alarm.
h. Oil filter differential pressure alarm.
i. Inlet separator level shutdown.
j. Cylinder lubrication protection.
k. Jacket water protection.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
35. Instrumentation data sheets.
36. Pulsation suppression device detail drawings and final pressure code calculations.
37. Special tools list (see 7.11.1). List of special tools furnished for maintenance.
38. Fabrication, testing and delivery schedule (see Item 42). Milestone fabrication, testing and delivery schedule, including
vendor buyouts.
39. Drawing list including latest revision numbers and dates.
40. Weather protection and climatization required.
41. Comments on purchaser’s piping and foundation drawings (see 6.1.16 and 7.7.1.6).
42. Progress reports (see 9.3.5). See Item 38, including:
a. Planned and actual milestone dates.
b. Engineering and manufacturing information on all major components.
c. Details of causes of delays.
43. Torsional analysis report, (see 6.7.1 and 7.1.2.6) including but not limited to the following:
a. Complete description of method used.
b. Graphic display of mass elastic system.
c. Tabulation identifying the mass moment and torsional stiffness for each component identified in the mass elastic system.
d. Graphic display of exciting forces versus speed and frequency.
e. Graphic display of torsional critical speeds and deflections (mode shape diagram).
f. Effects of proposed changes on analysis.
g. Current pulsation analysis.
44. Data for an independent torsional analysis.
45. Acoustic and mechanical analysis report, (see 7.9 and Annex M) including but not limited to:
a. Design approach (see 7.9.4.2.1) and method used (complete description), including description of design techniques used.
b. Findings and comparison with permitted values.
c. Effects of required modifications; and marked up drawings showing changes.
d. Other information as required by Annex M.
46. Data required for third-party acoustic and mechanical analysis. Information described in Annex M.
Note: It is the purchaser’s responsibility to provide some of the information described.
47. Engineering analysis for fabricated cylinders (see 6.15.5.1).
48. Balancing data tabulation. Listing of mass balance data for each throw, including piston, rod, crosshead, nuts, bushings,
bearings and balance masses and including both design target masses and actual assembly masses. The allowable mass tolerance
per throw shall be stated.
49. Valve dynamics report (see 6.9.1.9).
50. Data for an independent valve dynamic analysis.
51. Connection sketches (see 6.15.7.6).
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
145
52. Coupling-to-shaft alignment diagram. Shaft alignment diagrams (vertical and horizontal), including recommended coupling
limits during operation. Note all shaft-end position changes and support growths from 15ºC (60°F) ambient reference temperature
or other reference temperature specified by the purchaser. Include the recommended alignment method and cold setting targets.
53. As-built dimensions and data, including:
a. Fits, clearances and runouts measured during final assembly.
b. Nameplate data for each cylinder.
c. Cylinder minimum and design clearances for each end of each cylinder.
d. Volume of all clearance pockets, plugs or bottles installed on each cylinder.
e. Crank angle phasing.
a. Section 1—Compressor
1. Items 1, 2, 3, 40, 52.
2. Grouting (see 7.5.3.8).
3. Setting equipment, rigging procedures, component masses and lifting diagram.
4. Dismantling clearances.
5. Preservation and storage requirements (see 8.4.2).
6. Field assembly procedures, including frame and cylinder alignment requirements.
b. Section 2—Driver
1. Storage and preservation.
2. Setting gear, rigging procedures, component masses and lifting diagram.
3. Piping recommendations.
4. Composite outline drawing for driver including anchor bolt hole locations.
5. Dismantling clearances.
6. Thermal and mechanical movements of frame and shaft.
7. Motor air gap data (see 7.1.2.13).
c. Section 3—Gear
1. Storage and preservation.
2. Setting gear, rigging procedures, component masses and lifting diagram.
3. Piping recommendations.
4. Composite outline drawing for gear including anchor bolt hole locations.
5. Dismantling clearances.
6. Thermal and mechanical movements of casing and shaft.
d. Section 4—Auxiliary equipment
1. Storage and preservation.
2. Setting equipment, rigging procedures, component masses and lifting diagram.
3. Piping recommendation.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
54. Hydrostatic and gas test certificates (see 8.3.2).
55. Certified mechanical run test data (if test ordered).
56. Certified performance test data (if test ordered).
57. Non-destructive test procedures for fabricated cylinders.
58. Procedures for any special or optional tests (if tests ordered).
59. Certified data from special or optional tests (if test ordered) (see 8.3.4.1).
60. Certified mill test reports of Items as agreed in the pre-commitment or pre-inspection meeting(s). Physical and chemical data.
61. Crankshaft ultrasonic test certificate (see 8.2.2.3.3).
62. Valve leak test certificate.
63. As-built data sheets for compressor, gear, driver and auxiliary equipment, including gas data (see 6.1.23).
64. Installation manual (see 9.3.7.2) describing the installation requirements for the complete train, including the drawings
necessary for assembly of the equipment and location of field connections and including but not limited to the following:
146
API STANDARD 618
65. Operation and maintenance manual, (see 9.3.7.3) describing the operating and maintenance procedures, requirements and
limitations for the complete train and auxiliary equipment, including but not limited to the following:
a. Section 1— Operation
1. Initial commissioning and start-up, including final tests and checks.
2. Normal start-up.
3. Normal shutdown.
4. Emergency shutdown.
5. Operating limits, including Item 13 above.
6. Lube-oil recommendations, including injection rates and specifications.
7. Routine operational procedures.
8. Items 22, 30, 34 and 71.
b. Section 2—Maintenance, disassembly, repair and reassembly instructions for the complete train and auxiliary and accessory
equipment including but not limited to the following:
1. Valve overhaul data.
2. Cylinder overhaul data.
3. Table of bolt torques. The required torque values or elongations for tensioning the valve cover, valve hold down bolts,
connecting rod and main bearing bolts, piston and crosshead nuts, flange bolts and any other bolts that the vendor feels are
critical. Data should be included for fasteners in both the lubricated and non-lubricated condition.
4. Fits and clearances for wearing parts, recommended, maximum and minimum.
5. Items 4, 8, 19, 21, 37, 48, 52, 53 and 63.
6. Routine maintenance requirements.
7. Maximum allowable crankshaft web deflection.
c. Section 3—Performance Data. Items 7, 9 and 10.
d. Section 4—As Built Data. Items 53 and 63.
e. Section 5—Drawing and Data
1. Drawings in the manual shall be for the specific equipment supplied. Typical drawings are unacceptable.
2. Items 1, 5, 6, 8, 11, 15, 16, 19, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 36 and 39.
66. Technical Data Manual. See 9.3.7.4.
Technical and quality control data for technical support personnel for the complete train and auxiliary equipment, including but
not limited to:
67.
68.
69.
70.
71.
Procedures for preservation, packing and shipping.
Shipping list, including all major components that will ship separately.
Material safety data sheets. Description of the hazardous and potentially hazardous materials included in the scope of supply.
Quality plan. In accordance with ISO 9000 series.
Control logic diagram (see 7.6.2.3).
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Items 1 – 16, 18 – 20, 23, 26, 29 – 31, 33 – 37, 39 – 40, 43, 45 – 49, 52 – 63.
Annex G
(normative)
Figures and Schematics
G.1 General
The schematics presented here illustrate the general philosophy and requirements of this standard and are typical of commonly
used systems: they are not intended to include all details such as vent and drain details and minor piping connections to permit
disassembly. The systems may be modified as necessary with the agreement of the purchaser and vendor.
Instrument piping and valving details are not shown on typical schematics. Such requirements, including on-line testing
requirements, shall be agreed upon by the purchaser and vendor.
Requirements for all of the systems illustrated here are covered in the main text, as indicated by the cross-references in the notes
accompanying each figure. Further elaboration on the details of pressure packing to minimize process gas emissions is given in
Annex I.
G.2 Legend for Schematics
The abbreviations and symbols used in the schematics in this annex are defined below.
Letter
A
C
D
E
F
G
H
I
L
O
P
S
T
V
Y
First Letter
Analysis
Conductivity (Electrical)
Density (Sp. Gr.)
Voltage (EMF/Electrical)
Flow
Gauging (Dimensional)
Hand Actuated (Manual)
Current (Amps)
Level
(Unclassified)
Pressure/Vacuum
Speed/Frequency
Temperature
Vibration/Viscosity
(Unclassified)
147
Subsequent Letters
Alarm
Controller
Differential
Element (Primary)
Ratio (Fraction)
Glass/Gauge
High
Indicator
Light/Low
Orifice (Restriction)
Point
Safety/Switch
Transmitter
Valve
Relay
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
G.2.1 FLOW DIAGRAM IDENTIFICATIONS LETTERS
148
API STANDARD 618
G.2.2 SYMBOLS
,).% !.$ 0)0).' 39-"/,3 )$%.4)&)#!4)/.
0IPING LINE BY VENDOR
0IPING BY CONTRACTOR OR USER
0ROCESS INSTRUMENT LINE
)NSTRUMENT PNEUMATIC LINE
%LECTRICAL SIGNAL
(YDRAULIC SIGNAL
-!.5!,,9 /0%2!4%$ 6!,6%3
'ATE VALVE
#HECK VALVE
'LOBE VALVE
#/.42/, 6!,6%3
2EGULATOR
SELF CONTAINED
4#6
0#6
3PRING DIAPHRAGM
ACTUATED VALVE
FAIL OPEN
&/
4EMPERATURE
CONTROL
VALVE
-)3#%,,!.%/53 39-"/,3
&ULL FLOW
INLINE FILTER
(ORIZONTAL CENTRIFUGAL PUMP
MOTOR DRIVEN
(EAT EXCHANGER
WITH VENT AND
DRAIN VALVES
0IPE CAP
9 TYPE STRAINER
WITH PLUGGED
BLEED VALVE
6ALVE SIX PORT
CONTINUOUS FLOW
TRANSFER MANUALLY
OPERATED
0IPE UNION
&)
6ARIABLE AREA
FLOW INDICATOR
3HUTDOWN
INTERLOCK
026
0RESSURE RELIEF
VALVE
0IPE PLUG
2/
2ESTRICTION ORIFICE
0IPE UNION
,OCAL PANEL
MOUNTED PILOT
LIGHT
,OCAL MOUNTED
INSTRUMENT
,OCAL PANEL
MOUNTED INSTRUMENT
#3/ n #AR 3EAL /PEN
&/ n &AIL /PEN
./ n .ORMALLY /PEN
)
s9
0
#URRENT TO
PNEUMATIC
RELAY
s 2ELAY
VARIABLE
TYPE
!""2%6)!4)/.3
/73 n /ILY 7ATER 3EWER
&# n &AIL #LOSED
.# n .ORMALLY #LOSED
--``,,,``,,`````,``,,,,,,,`,,`,,
Drain
OWS
Compressor
cylinder
Figure G-1—Cylinder Cooling System
In
Heater
(see caution
note)
Unions
Compressor
cylinder
FI
PLAN C
FORCED COOLING SYSTEM
Drain
OWS
TI
PLAN A
STATIC (STANDPIPE) SYSTEM
Adequate
expansion
chamber
with full
mark
LG
Out
Vent
PLAN B
THERMOSYPHON SYSTEM
Cooler (finned pipe
typical, inclined for
maximum effectiveness)
Compressor
cylinder
Drain
OWS
In
Out
CAUTION: When jacket water temperature is to be
controlled by steam sparging, the following
precautions should be observed:
a. A silent (water-hammer-cushion type) steam
sparger should be placed in the water inlet line to the
jacket system.
b. The water flow rate must remain constant in
accordance with the manufacturer's requirements.
c. The steam flow into the water should be regulated
automatically to maintain the water jacket
temperatures in accordance with 6.8.3.5.2.
PSL
PI
Jacket water
system failure
alarm
PAL
TCV
Drain
Outer head
Cylinder
Drain
Vent
Cooler
Note 6
TI
Aux. pump
TI
Water console
outlet connection
Drain
Compressor A
Note 8
Vent
FI
FI
TI
Vent
TI
FI
Main pump
Jacket water coolant console
Drain
Note 9
FI
Vent
PLAN D
JACKET WATER COOLING SYSTEM
Vent
TI
Figure G-1—Cylinder Cooling Systems
TI
Frame
head
Vent
Frame
head
LG
Notes:
1. Instrumentation shown is minimum required. The
purchaser may wish to specify additional devices.
2. Flow through cylinders may be either series or
parallel.
3. See 6.8.3 and 7.7.4.
4. Heaters used to preheat the cylinder cooling water
(if needed to meet the requirements of 6.8.3.4.2 or
6.8.3.5.2) may be electric, hot water, or steam. They
must be sized to take into account heat losses of
surface areas of the cylinder, pipe, and fittings. Good
judgment must be exercised so that heaters will not
be undersized.
5. Normal level is above the highest point of the
cylinder piping.
6. Cooler to have vents and drains on both shell and
tube side.
7. The system shown is typical: more or less
equipment may be furnished.
8. Series flow.
9. Parallel flow.
TI
Cylinder
Coolant
level
Vent and fill
connection
Outer head
TI
See Note 2
Outer head
Drain
Vent
Drain
Reservoir
Note 5
Normal
level
Compressor B
Note 8
Vent
FI
Console boundary
RO
Drain
Vent
Vent
Frame
head
Adequate
expansion
chamber
FI
TI
Vent
Drain
Drain
Cleanout
connection
Heater
LG
FI
Note 9
Fill
connection
TI
Vent
Frame
head
Coolant
level
Vent
TI
FI
Water console
return connection
Cylinder
Vent and fill
connection
Outer head
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Vent is stainless
steel tube 1/2 inch
minimum
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
149
Cylinder
150
API STANDARD 618
Cylinder
water jacket
Liner
Straight
threads
17-4 PH stainless
steel sleeve
Boss
Cylinder body casting
Wrench flats
Soft steel
gasket
1/2" NPT
Note 1: See 6.8.4.1.16
Note 2: This typical arrangement utilizes a 17-4 stainless steel sleeve as a standard compressor cylinder design. The sleeve is installed during
manufacture of the cylinder, providing a high-strength, corrosion resistant passage through a minor boss area. The design installation arrangement of the 17-4 stainless steel sleeve may vary among manufacturers.
Figure G-2—Typical Cylinder Indicator Tap Connection
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
1
E
C
B
(When required)
Access
opening
Distance
piece
D
F
B
(When required)
A
G
Pressure
packing
Cylinder
P
C
B
D P
Oil slinger
2 (see note 4)
1
Access
opening
B
Inboard
distance piece
B
(When required)
A
P
Access
opening
P
E
D
C
(When required)
Outboard
distance piece
P
Intermediate
partition
Piston
B
Figure G-3—Distance Piece and Packing Arrangements
F
A
G
Pressure
packing
(When required)
Cylinder
Piston
1
Access
opening
P
C
B
D P
Oil slinger
2 (see note 4)
B
(When required)
Inboard
distance piece
B
D
C
B
(When required)
Distance piece
Oil slinger
Access
opening
E
(When required)
1
B
F
A
G
Pressure
packing
A
P
E
D
C
(When required)
P
Intermediate
partition
B
F
A
G
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Cylinder
Piston
Piston
Cylinder
Outboard
distance piece
Pressure
packing
Access
opening
(optional)
(When required)
TYPE B
LONG SINGLE-COMPARTMENT DISTANCE PIECE
(SUFFICIENT LENGTH FOR OIL SLINGER TRAVEL)
Crosshead guide
Crosshead
Piston rod
Oil wiper packing
(see note 3)
B
TYPE D
SHORT TWO-COMPARTMENT OR DOUBLE DISTANCE PIECE ARRANGEMENT
(INBOARD DISTANCE PIECE OF SUFFICIENT LENGTH FOR OIL SLINGER TRAVEL)
Crosshead guide
Crosshead
Piston rod
Oil wiper packing
(see note 3)
Frame end
Partition
Partition
Frame end
3. The oil wiper packing may be located in the distance piece on the other
side of the partition from that shown, and would be an integral assembly
with the seal or buffer packing (1).
4. The intermediate seal or buffer packing (2) may be located in the outboard
distance piece on the other side of the partition from that shown.
Connections (see 6.12.2 for sizes):
A Vent, distance piece
B Purge, buffer, or pressure, packing or distance piece
C Lube, pressure packing
D Drain, distance piece
E Coolant out, pressure packing
F Coolant in, pressure packing
G Common vent and drain, pressure packing
P Plugged connection
Legend:
1. Seal or buffer packing, distance piece
2. Intermediate seal or buffer packing, distance piece (solid access
covers required)
Notes:
1. See 6.10 and 6.13.1.3.
2. The orientation of distance-piece and packing-flange/case connections
may vary depending on the individual distance piece and the type of
packing case used.
TYPE C
LONG TWO-COMPARTMENT OR DOUBLE DISTANCE PIECE ARRANGEMENT
(INBOARD AND OUTBOARD DISTANCE PIECES EACH OF SUFFICIENT
LENGTH FOR OIL SLINGER TRAVEL)
Crosshead guide
Crosshead
Piston rod
Oil wiper packing
(see note 3)
Frame end
Partition
TYPE A
SHORT SINGLE-COMPARTMENT DISTANCE PIECE
(MAY BE INTEGRAL WITH CROSSHEAD GUIDE OR CRANK END HEAD)
Crosshead guide
Crosshead
Piston rod
Oil wiper packing
(see note 3)
Frame end
Partition
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
151
152
API STANDARD 618
4)
4)
6ENT
4)
6ENT
6ENT
&)
&)
%
&)
%
#OMPRESSOR 0RESSURE
#YLINDER
0ACKING
%
#OMPRESSOR 0RESSURE
#YLINDER
0ACKING
&
#OMPRESSOR 0RESSURE
#YLINDER
0ACKING
&
&
.OTE .OTE $RAIN
.OTE $RAIN
#ONSOLE COOLANT
SUPPLY CONNECTION
$RAIN
#ONSOLE COOLANT
RETURN CONNECTION
#ONSOLE BOUNDARY
0!,
&ILL
CONNECTION
)NLET CONNECTION
03,
0)
0URGE
CONNECTION
6ENT TO A
SAFE AREA
.ORMAL
LEVEL
6ENT
4)
,'
.OTE 4)
2ESERVOIR
CLEANOUT
CONNECTION
$RAIN
-)#2/.
&),4%2
#//,%2
.OTE $RAIN
2%3%26/)2
0)
0)
!58 05-0
-!). 05-0
0ACKING COOLING CONSOLE FOR COOLANT
Note 1: The instrumentation shown is the minimum required. The purchaser may wish to specify additional devices.
Note 2: For cooling medium other than water system design shall be mutually agreed upon between purchaser and the vendor.
Note 3: See 6.13.
Note 4: If a packing cooling console is not supplied, individual strainers are required (see 6.13.2.6).
Note 5: Cooler to have vents and drains on both shell and tube side.
Note 6: Normal level is above the highest point of the piping on the compressor cylinders.
Note 7: The system shown is typical: more or less equipment may be provided.
Figure G-4—Typical Self-Contained Cooling System for Piston Rod Pressure Packing
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
153
Console boundary
PDAH
Notes:
1. Instrumentation shown is
the minimum required. The
purchaser may wish to
specify additional devices.
2. See 6.14.2.
3. Cooler to have vents and
drains on both shell and
tube side.
4. The system shown is
typical: more or less
equipment may be provided.
5. Check valve with RO on
main pump is optional. The
RO is for priming the main
pump.
6. See 6.14.2.4.
7. Six-port continuous-flow
transfer valve, manually
operated.
PDSH
Vent
Note 6
Oil
filter
TI
Drain
TCV
Note 3
Manual
override
Note 7
Vent
RO
OIL
COOLER
Oil
filter
TI
PRV
Drain
RO
Note 5
Motor
Console
return connection
Oil system
extended to driver
(if specified)
AUX. PUMP
Console
supply
connections
Aux. pump start
I
Shutdown
I
PI
PSLL
PAL
PSL
PSL
Frame
breather
RO
PRV
Main
drive
motor
Main
pump
LG
LAL
LSL
Inlet
strainer
FI
CRANKCASE OIL RESERVOIR
Gravity drain to
crankcase (when oil
system extended to
driver is specified)
Heater
Crankcase
drain
Drain
OWS
Figure G-5—Typical Pressurized Frame Lube Oil System
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Note 6
154
API STANDARD 618
Jambnut
Body (Crosshead)
Location of
thread-root prestressforce
Bolt (Piston rod)
Figure G-6—Conceptual Direct Rod Connection
Bolt (Piston rod)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Body (Crosshead)
Figure G-7—Conceptual Indirect Rod Connection
Clamping Nut
Body (Crosshead)
Bolt (Piston rod)
Figure G-8—Conceptual Indirect Clamped Rod Connection
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
155
Body (Crosshead)
characteristic
Force
Bolt (Piston rod)
characteristic
Operating Force
during compression stroke
Fo
Fp
Fa
Prestress Force
of Fastening
Fo
Fp
Operating Force
during tension stroke
Fm
Fr
Definitions:
Fp = Prestress of the Fastening
Fo = Operating Force (under MAWP-condition, or at maximum allowable continuous rod load)
Fa = amplitude of the alternating Force (in the bolt-shaft and thread)
Fm = max Force (in the bolt-shaft and thread)
Fr = min remaining Force in the fastening
Smax = max stress in the thread-root or any other area of the bolt due to Fm
Sa = alternating Stress at the thread-root section due to Fa
Figure G-9—Tightening Diagram (Bolt–Bracing–Diagram)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Elongation
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex H
(Informative)
Materials for Major Component Parts
Table H-1—Material Specifications for Reciprocating Compressor Parts
Part
Material
Frame
Crankshafts
Connecting rods
Crossheads
Cast iron
Steel
Steel
Steel
Ductile iron
Crosshead pins
Steel
Distance pieces
Cast iron
Cylinders
Steel
Stainless steel
Nodular iron
Gray iron
Cylinder liners
Steel
Stainless Steel
Ni-resist
Nodular iron
Gray iron
Cylinder heads
Steel
Stainless steel
Nodular iron
Gray iron
Pistons
Steel
Cast iron
Aluminum
Piston rods and tailrods
Steel
Stainless Steel
Piston rod nuts
Steel
Stainless Steel
Valve seats and guards
Steel
Stainless steel
Nodular iron
Cast iron
Valve plates
Stainless steel
Non-metallic
Valve springs
Steel
Stainless steel
Packing cases
Steel
Stainless steel
Cast iron
Packing case flange
Steel
Piston rings, wear bands, and packing rings Metallic
Non-metallic
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
157
Form
Cast
Forged
Forged
Bar stock, forged, or cast
Cast
Forged or bar stock
Cast
Cast, forged, or fabricated
Cast or fabricated
Cast
Cast
Tubing
Cast
Cast
Cast
Cast
Cast, forged, or fabricated
Plate
Cast
Cast
Forged, cast, bar stock, or fabricated
Cast
Forged or cast
Forged or bar stock
Bar stock
Forged or bar stock
Forged or bar stock
Plate or bar stock
Plate, bar stock, or cast
Cast
Cast
Plate
Molded
Drawn
Formed
Bar stock
Bar stock
Cast
Forged, bar stock, or plate
Cast or Bar Stock
Molded or Sintered
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex I
(informative)
Distance Piece Vent, Drain and Buffer Systems to Minimize Process Gas Leakage
I.1 Scope
This annex contains a general philosophy for the design of reciprocating compressor distance piece vent, drain, and gas buffer
systems, which are typical of systems commonly used to minimize process gas leakage. This annex is not intended to cover all
possible situations; rather, it focuses on providing an approach, which can be used to design successful systems.
Note: The piping, tubing, and components external to the distance piece may be supplied by either the purchaser or vendor. It is good practice
for the vendor and purchaser to discuss the vent and drain system, and agree on its design (see 6.12.2).
Instrument piping and valving details are not shown on typical schematics. Such requirements, including on-line testing
requirements, should be agreed upon by the purchaser and vendor.
I.2 Abbreviation and Symbols
The abbreviations and symbols used in the schematics in this annex are shown in Annex G.
I.3 The Purpose of Distance Piece Vent, Drain and Buffer systems
A distance piece vent and drain system working in conjunction with packing, buffer system and partitions, accomplishes several
functions, including:
a. confining and collecting the normal leakage from compressor rod pressure packing and carrying the leakage to a safe location;
b. preventing process gas, toxic gas or hazardous gas leakage into the area around the machine;
c. preventing contamination of the crankcase lube oil;
d. atmospheric fugitive emission control;
e. confining and collecting large leakage in the event of compressor pressure packing failure, and directing the leakage to a safe
location;
f. helping to prevent an explosive atmosphere from developing in the crankcase;
g. preventing excessive liquid accumulation in the distance piece;
h. avoiding gas leakage to sewer systems;
i. allowing the operator to monitor and determine the condition of compressor rod pressure packing.
I.4 Minimizing Process Gas Leakage
Figures I-1 and I-2 illustrate the arrangement of two typical distance piece types that may be used when it is necessary to reduce
the leakage of process gas to a minimum. The accompanying packing detail drawing, Figure I-3, shows the arrangement of the
packing rings and the direction of flow and typical pressures of the buffer gas.
Side-loaded packing rings provide constant mechanical axial loading towards the sealing face of the cup. This mechanical axial
loading, added to a buffer gas pressure at least 1 bar higher than the disposal pressure, hold the rings positively against their
sealing faces minimizing buffer gas leakage and, at the same time, assures that all the process gas that leaks past the cylinder
pressure packing cups will be forced out into the disposal system (for example, the flare) through the vent.
When proper differential buffer gas pressures are maintained, process gas leakage into the distance pieces is minimal; process gas
is prevented from entering the compressor frame. To minimize gas emissions, special packing and long distance pieces should be
specified (see 6.13.1.6).
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
159
160
API STANDARD 618
I.5 Design Consideration
In addition to meeting the purposes described in I.2 the following factors should be considered when designing in designing a
distance piece vent, drain and buffer system:
a. Small diameter vent and drain piping will tend to foul and corrode over time, inhibiting their function. Consider using large
[e.g., DN 50 (NPS 2)] vent and drain headers and corrosion-resistant materials.
b. On two-compartment distance piece systems, external cross connections between the inner and outer compartment vents and
drains should be avoided.
c. On multiple machine systems, it should be possible to isolate each machine for maintenance.
d. Effective control of gas leakage requires the specification of gasketed solid metal covers on distance pieces (see 6.12.2.1).
e. Where vents, drains, liquid collection pots and distance pieces are connected to disposal systems, such as a flare or closed
drain system, they should be designed to withstand the maximum disposal system pressure (e.g., flare back pressure under
relieving conditions). See 6.12.2.3.
Note: Distance pieces are typically designed for a maximum gauge pressure of 2 bar (25 psi). Special designs are required for higher pressures.
f. Typically, the common vent and drain from the pressure packing (connection G in Figure I-1 and I-2) will be carrying a
mixture of liquid and gas. The system should be designed to separate these phases to avoid liquid blockage of the vent system.
g. Leaks from the stems of valve unloaders and clearance pockets may also need to be collected and controlled. These can be
integrated with the distance piece vent and drain system.
h. There is concern about the reliability of check valves in safety situations, particularly in low pressure systems such as distance
piece vent and drain systems where there is any mixture of gas and liquids. Check valve use should be avoided, where possible.
i. Except for the pressure packing combined vent and drain, which is a pressure driven flow, separate vent and drain lines are
necessary between the distance piece and liquid collection pot to pressure balance the system and allow free drainage. Sloped
headers, without pockets, assist draining.
j. Large diameter tubing [20 mm (3/4 in.) OD minimum] can be used between the individual distance pieces and the vent and
drain headers. This usually results in a neat, easily maintained installation compared to a piping system.
k. Manifolding and cross-connections with drains and blowoffs from other equipment should be avoided.
l. The buffer gas purge pressure must be limited to the maximum allowable pressure for the distance piece components (see
6.10.4). Some buffer gas will flow into the compressor frame. Frame venting must allow an outlet for this flow (see Figure G-5).
m. Pneumatic trip systems internal to the frame (e.g., crosshead pin temperature) should be energized with nitrogen rather than air
to assist in maintaining an inert atmosphere in the crankcase.
n. Effective establishment of an inert atmosphere in the crankcase will necessitate special maintenance safety procedures.
o. Where climatic conditions require, drains should be heat-traced and insulated.
p. Under total packing failure, it should not be possible to over-pressure the distance piece (see 6.10.4 and 6.10.5). If the vent area
is not sufficient, additional venting to a safe location by way of emergency pressure relief valves or spring-loaded pressure relief
doors may be required.
q. Buffer gas purge rates are typically sized for a flow rate of 0.03 m3/h (10 standard ft2/h) per packing set [may reach 0.2 m3/h
(65 standard ft2/h) per packing set on startup] and are fitted with flow indicators.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Pressure
packing
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
From other
cylinders
(note 9)
Monitoring TI
Cylinder
Piston
Electrical signal
Typically, all components external to distance piece or as shown in
broken line – – – – – are furnished by purchaser.
-----------
G
F
5-50 SCFH
PRV
PI
PI
FI
5-50 SCFH
PSL (note 6)
Slope
To other
cylinders
(note 9)
Buffer gas (note 2)
Distance piece vent [see I.5(i)]
To other
cylinders
(note 9)
5-50 SCFH
FI
PSL (note 6)
PI
PI
PRV
5-50 SCFH
PCV
(note 2)
F
FI
PI
G
A
Pressure
packing
Filter
PDI
TE
Nom. 6 BAR
(100 PSIG)
Buffer gas supply
B
E
B
B
Slope
Frame end
Slope
TYPE A DISTANCE PIECE
Crosshead guide
Piston rod
Crosshead
Oil wiper packing
(see note 3)
Note:
This is a typical system and may
require modification based on
specific user requirements
(see I.1).
Leak offs from cylinder and clearance
pocket unloaders. (optional - note 9)
D
Access opening
(solid cover)
(1)
Outboard
distance piece
NO
C
Partition
Distance piece
liquid collection pot
Distance piece drain
NC
LG
Oil slinger
D
E
NO
C
To disposal system
(e.g. vapor recovery
or low pressure flare)
(see note 8)
Slope
Oil and condensate
drain
Slope
Pressure packing combined vent and drain
B
Access opening
(solid cover)
Outboard
distance piece
(1)
B
TYPE B DISTANCE PIECE
Crosshead guide
Piston rod
Crosshead
Oil wiper packing
(see note 3)
Frame end
Partition
B
Cylinder
Slope
Monitoring
From other
cylinders
(note 9)
PI
NC
Oil and condensate
drain
LG
Packing leakage
liquid collection pot
Notes:
1. See 6.12.2 and 6.13.1.6
2. Buffer gas pressure must be at least 1 bar (15
pounds per square inch) higher than the
disposal system pressure at connection A or
connection G (in the outboard distance piece)
whichever is higher.
3. The oil wiper packing may be on the distance
piece side of the partition and integral with the
buffer seal packing (1).
4. In some cases, lower buffer and vent
pressures than the examples shown in the
packing details may be necessary to
accomodate the pressure limitations of large
distance pieces.
5. Several other distance piece and packing
arrangements for pressuring, buffering,
purging, and venting are possible, and the
arrangement to be used should be agreed upon
between the purchaser and the vendor.
6. Some users may choose to shutdown as well
as alarm in some cases.
7. Fixed pressure control or differential pressure
control depending on the variability of the
disposal system.
8. Keep the disposal from the distance piece
liquid collection pot and packing leakage liquid
collection separate. The distance piece liquid
collection pot should be connected to a vapor
recovery system or a low pressure flare system.
The packing leakage liquid collection pot can
be connected to either a vapor recovery, a low
pressure flare, or a conventional flare system.
9. To or from other cylinders on the same
machine. When different cylinders on a
common frame are in different services,
individual isolation of vents and drains may be
required.
To disposal system
(note 8)
Intended Mode of Operation
• The distance piece operates at disposal system pressure-usually a gauge pressure of 0.15 to 0.4 bar (2 to 5
pounds per square inch) and is filled with a mixture of inert buffer gas and process gas. The packing vent TI
allows monitoring of the packing condition. There is normally no process gas leakage into the distance
piece. Under abnormal conditions (such as packing deterioration), the rate of leakage of process gas into
the crosshead guide is dependent on the condition of the pressure packing and the buffer seal packing (1).
• Alternatively, the disposal system may be operated at a vacuum, at an absolute pressure of 0.7 to 0.9 bar
(10 to 13 pounds per square inch), based on an atmospheric pressure of 1 bar (14.7 pounds per square
inch), in which case the crosshead guide leakage may be into the distance piece, and a pump could be
needed for the distance piece liquid collection pot drain.
• The liquid collection pots will require occasional draining.
• The distance piece vent header PSH is set to alarm (or shutdown) if the pressure packing on one cylinder
fails.
TI
Piston
TI
FI
DPCV
Monitoring
A
PI
TI
TE
PCV
FOR CONSTANT PRESSURE DISPOSAL SYSTEMS – NOTE 7
Monitoring
Filter
PDI
Legend:
A Vent, distance piece – NPS 1.50
B Purge, buffer, or pressure, packing or distance piece – NPS 1.00
C Lube, pressure packing – NPS 1.00
D Drain, distance piece – NPS 1.00
E Coolant out, pressure packing – NPS 1.00
F Coolant in, pressure packing – NPS 1.00
G Common vent and drain, pressure packing – NPS 1.00
(1) Buffer seal packing
(2) Intermediate partition packing
From other
cylinders
(note 9)
(note 6)
PSH
Nom. 6 BAR
(100 PSIG)
Buffer gas supply
(note 2)
FOR VARIABLE PRESSURE DISPOSAL SYSTEMS – NOTE 7
PI
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
161
Figure I-1—Typical Buffered Single Compartment Distance Piece Vent, Drain, and Buffer Arrangement to Minimize
Process Gas Leakage
TE
G
B
FI
F
PI
A
PI
PSL (note 9)
PSL
B
PI
From other
cylinders
(note 13)
Outboard
distance piece
B
B
NC
D
Slope
FG
B
(1)
B
FI
Crosshead
Slope
Slope
Distance piece
liquid collection pot
To other
cylinders
(note 13)
5-50 SCFH
NC
Oil and condensate
drain
To disposal system
(e.g. vapor recovery
or low pressure flare)
(note 12)
Slope
From other
cylinders
(note 13)
Pressure packing combined vent and drain
B
FI
PI
B
PI
NC
A
PRV
A
E
To
drain
D
Slope
Outboard
distance piece
F
B
FI
PCV
(note 2)
C
NO
Access opening
(solid cover)
B
PI
Intermediate
partition
PRV
G
Electrical signal
PI
Nom. 6 BAR
(100 PSIG)
Buffer gas supply
Piston
TI
Monitoring
Filter
Oil and condensate
drain
NC
LG
Packing leakage
liquid collection pot
To disposal system
(note 12)
Cylinder
TE
PDI
Typically, all components external to distance piece or as shown in broken line – –
– – – are furnished by purchaser.
-----------
TI
(Monitoring)
Pressure
packing
5-50 SCFH
PI
Legend:
A Vent, distance piece – NPS 1.50
B Purge, buffer, or pressure, packing or distance piece – NPS 1.00
C Lube, pressure packing – NPS 1.00
D Drain, distance piece – NPS 1.00
E Coolant out, pressure packing – NPS 1.00
F Coolant in, pressure packing – NPS 1.00
G Common vent and drain, pressure packing – NPS 1.00
(1) Buffer seal packing
(2) Intermediate partition packing
FG
D
(2); (note 4)
Access opening
(solid cover)
B
PI
Optional inboard
distance piece purge
B
PCV
PSL (note 9)
PRV
FOR CONSTANT PRESSURE DISPOSAL SYSTEMS – NOTE 11
Optional intermediate partition
packing purge
Oil slinger
(1)
Inboard
distance piece
TYPE D DISTANCE PIECE
Crosshead guide
Piston rod
Crosshead
Oil wiper packing
(note 3)
Frame end
Partition
Outboard distance piece drain
LG
(note 9) PSL
To other cylinders
(note 13)
Buffer gas pressure P2 (notes 2, 10)
Inboard distance piece drain
TYPE C DISTANCE PIECE
Crosshead guide
Piston rod
Oil wiper packing
(note 3)
Frame end
Partition
5-50 SCFH
Distance piece vent [see I.5 (i)]
Inboard
distance piece
Oil slinger
Access opening
(solid cover)
(2); (note 4)
Slope
A
PI
To other
cylinders
(note 13)
Buffer gas pressure P1 (note 2)
(note 9)
Optional intermediate partition
packing purge
Intermediate
partition
Optional inboard
PRV
distance piece purge
PRV
Access opening
(solid cover)
D
E
NO
C
DPCV
(note 2)
Leak offs from cylinder and clearance
pocket unloaders. (optional - note 13)
TI
(Monitoring)
Pressure
packing
From other
cylinders
(note 13)
Cylinder
Piston
TI
5-50 SCFH
PCV
PI
To other cylinders
(note 13)
Intended Mode of Operation
• The inboard distance piece is full of inert buffer gas and will stabilize at a gauge pressure of 0.7 to 1 bar (10 to 15 pounds per square
inch). Infrequent oil draining is required.
• The outboard distance piece operates at disposal system pressure-usually a gauge pressure of 0.15 to 0.4 bar (2 to 5 pounds per
square inch) and is filled with a mixture of buffer gas and process gas. The packing vent TI allows monitoring of the packing
condition. There is normally no process gas leakage into the distance piece. Under abnormal conditions (such as packing
deterioration), the rate of leakage of process gas into the crosshead guide is dependent on the condition of the pressure packing, the
intermediate partition packing (2), and the buffer seal packing (1).
• Alternatively, the disposal system may be operated at a vacuum, at an absolute pressure of 0.7 to 0.9 bar (10 to 13 pounds per
square inch), based on an atmospheric pressure of 1 bar (14.7 pounds per square inch), in which case the crosshead guide leakage
may be into the distance piece, and a pump could be needed for the distance piece liquid collection pot drain.
• The liquid collection pots will require occasional draining.
• The distance piece vent header PSH is set to alarm (or shutdown) if the pressure packing on one cylinder fails.
From other
cylinders
(note 13)
(note 9)
PSH
Filter
PDI
(Monitoring)
Nom. 6 BAR
(100 PSIG)
Buffer gas supply
PI
PCV
PRV
FOR VARIABLE PRESSURE DISPOSAL SYSTEMS – NOTE 11
Note:
This is a typical system and may
require modification based on
specific user requirements
(see I.1).
Notes:
1. See 6.12.2 and 6.13.1.6
2. Buffer gas pressure P1 must be at
least 1 bar (15 pounds per square
inch) higher than the disposal
system pressure at connection A or
connection G (in the outboard
distance piece) whichever is higher.
Buffer gas pressure P2 must be at
least 1 bar (15 pounds per square
inch) higher than the disposal
system pressure at connection A (in
the outboard distance piece).
3. The oil wiper packing may be on
the distance piece side of the
partition and integral with the
buffer seal packing (1).
4. The intermediate partition
packing (2) may be buffered in
addition to the pressure packing in
which case the inboard distance
piece may be vented to the
atmosphere.
5. In some cases, lower buffer and
vent pressures than the examples
shown may be necessary to
accomodate the pressure
limitations of large distance pieces.
6. Several other distance piece and
packing arrangements for
pressuring, buffering, purging, and
venting are possible, and the
arrangement to be used should be
agreed upon between the
purchaser and the vendor.
7. The orientation of the distance
piece and packing flange/case
connections may vary depending
on the individual distance piece and
the type of packing case used.
8. The intermediate partition
packing (2) may be located in the
outboard distance piece on the
other side of the partition from that
shown.
9. Some users may choose to
shutdown as well as alarm in some
cases.
10. Buffer gas may be fed either to
the buffer seal packing (1) as
shown, or directly into the inboard
distance piece.
11. Fixed pressure control or
differential pressure control
depending on the variability of the
disposal system.
12. Keep the disposal from the
distance piece liquid collection pot
and packing leakage liquid
collection separate. The distance
piece liquid collection pot should
be connected to a vapor recovery
system or a low pressure flare
system. The packing leakage liquid
collection pot can be connected to
either a vapor recovery, a low
pressure flare, or a conventional
flare system.
13. To or from other cylinders on
the same machine. When different
cylinders on a common frame are in
different services, individual
isolation of vents and drains may be
required.
162
API STANDARD 618
Figure I-2—Typical Buffered Two Compartment Distance Piece Vent, Drain, and Buffer Arrangement to Minimize
Process Gas Leakage
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
OIL WIPER PACKING WITH INERT BUFFER GAS PURGE
INTERMEDIATE PARTITION PACKING WITH INERT BUFFER GAS PURGE
(Not Used With Type A & B Distance Pieces)
B
Frame/distance
piece partition
163
Inert buffer
gas pressure P2
(see note 2)
Distance piece
intermediate
partition
Distance piece
side
B
Buffer gas
(see note 3)
Buffer gas
(see note 3)
Buffer gas
(see note 3)
Buffer gas
(see note 3)
Oil wiper
rings
Inert buffer
gas pressure P2
(see note 2)
Oil slinger
Outboard
distance piece
Inboard
distance piece
WTPR
(see note 4)
Oil drain back
to crankase
WTPR
(see note 4)
PRESSURE PACKING WITH INERT BUFFER GAS PURGE
Cylinder head
Cylinder side
Distance piece side
Inert buffer
gas pressure P1
(see note 2)
Notes:
1. See 6.12.2 and 6.13.1.6.
2. Buffer gas pressure P1 must be at least 1 bar (15 pounds per square
inch) higher than the disposal system pressure at connection A or G (in the
outboard distance piece) whichever is higher. Buffer gas pressure P2 must
be at least 1 bar (15 pounds per square inch) higher than the disposal
system pressure at connection A (in the outboard distance piece). See
Figures I-2 and I-3.
3. Under normal conditions, the buffer gas leakage rate is minimal. Under
abnormal conditions (such as packing deterioration), a higher buffer gas
leakage rate will occur.
4. WTPR = Wedge Type Packing Rings.
5.
= Sealing face of packing cups.
B
Buffer gas
(see note 3)
Process gas
Packing vent to disposal
system (flare) maximum
gauge pressure 1.5 bar
(25 psi)
Cylinder
gas pressure
G
WTPR (see note 4)
Figure I-3—Typical Purged Packing Arrangements
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex J
(informative)
Reciprocating Compressor Nomenclature
165
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Figure J-1—Reciprocating Compressor Nomenclature
Discharge valve
cage
Piston nut
Cylinder head
(outer end or
head end)
Discharge
valve
Piston rings
Cylinder liner
Port or Clearance
Pocket Unloader
(see 6.7.11)
Valve cover
Wear bands
(rider bands)
Plug Type
Unloader
(see 6.7.11)
Cylinder
Piston
Piston rod
Cylinder head
(frame end or crank end)
Connecting rod
Crankpin bearings
Frame
Crosshead guide
Oil slinger
Finger Type
Unloader
(see 6.7.11)
Cylinder
not
shown
Distance piece
Suction
valve
Crankshaft
PLAN VIEW
Frame
ELEVATION VIEW
Frame cover
Oil pump
end
Motor end
Crosshead
pin bushing
Piston rod
locknut
Crosshead
Piston rod
pressure packing
Intermediate
partition packing
Oil wiper
packing
Suction valve
cage
Connecting rod
pin bushing
Cylinder
not
shown
Crosshead
pin bushing
Crosshead shoe
Crosshead pin
Crosshead guide
Main bearings
Gas
discharge
Gas
inlet
Suction valve
unloaders
Unloader Rain
Cover
(see 6.7.11)
Clearance
pocket
unloader
Clearance
pocket
Suction
valve
Slot for
unloader
tubing
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
167
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex K
(informative)
Inspector’s Checklist
This inspector’s checklist represents a summary of the potential inspection points mentioned in the main text. The final inspection
plan shall be agreed between purchaser and vendor and reflected in the quality plan.
Table K-1—Inspector’s Checklist
Material Inspection
Crankshaft Ultrasonic Inspection
Piping Fabrication and Installation
Hydrostatic Test—Cylinders
Hydrostatic Test—Piping and Vessels
Gas Leakage Test
Shop Test
Bar-over Test Piston Rod Runout per Runout Table in Annex C
Cylinder Valve Leak Test
Additional Tests—As Specified
Crankshaft Web Deflection
Examination of Internals for Cleanliness:
Piping
Crankcase
Pulsation Suppressors
Coolers
Filters
Other
Rotation Arrow
Overall Dimensions and Connection Locationsa
Flange Dimensions and Finisha
Anchor Bolt Layout and Sizea
Painting
Corrosion Protection—Exterior
Referenced
Clause API 618 Date Inspected
8.2.2.1
8.2.2.3.3
Inspected By
Status
8.3.2.1
8.3.2.1
8.3.2.2
8.3.3.1
8.3.4.1
8.3.4.3
6.16.2
8.4.5
8.4.6
8.4.17
8.4.7
8.4.20
8.4.8
8.4.10
8.4.11
8.4.12
6.16.2
8.4.14
8.4.15
8.4.19
Corrosion Protection—Interior
Corrosion Protection—Lubricated Surfaces
Closures of All Openings
Equipment Nameplate Data
Packing for Shipment
Equipment Identification
Piping Connections Identification (Tagging)
Additional Inspections—As Specified
a Check against certified drawings.
169
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Item
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex L
(informative)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Figure L-1—Typical Mounting Plate Arrangement
171
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex M
(informative)
Design Approach Work Process Flowcharts
The work processes used in Design Approaches 1, 2 and 3 described in 7.9.4.2 are illustrated in Figures M-1, M-2 and M-3
respectively. The steps in the hierarchy of the Basic Criteria described in 7.9.4.2.5.2 are shown with circled numbers in each
figure.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Preliminary
pulsation
Preliminary Pulsation
supression device
Suppression
Device
Sizingper
per7.9.4.2.2.
7.9.2.3. If If
sizing
specified, minimum
minimum
specified,
volume shall
shall be
volume
be per
per
7.9.1.4
7.9.3.2.
Revise
Revise
design
Design
X
Show
the the
stepstep
in 7.9.4.2.5.2
Shows
in 7.9.2.6.2
1
No
Pulsation
Pulsation Criteria
criteria inin
7.9.2.6.2.2.1 and
7.9.4.2.5.2.2.1
andPressure
pressure
Drop
Criteria
in 7.9.2.6.3.1
drop
criteria
in 7.9.4.2.5.3.1
met?
Met?
Figure M-1—Design Approach 1
173
Yes
Yes
Design
DesignApproach
approach 11
Analysis
analysisComplete
complete
174
API STANDARD 618
Preliminary
pulsation
Preliminary Pulsation
suppression Device
device
Suppression
sizing
Sizingper
per7.9.4.2.2.
7.9.2.3. IfIf
specified,
minimum
specified,
p minimum
volume shall be per
7.9.1.4
7.9.3.2
X
Shows
thethe
step
in 7.9.4.2.5.2
Shows
step
in 7.9.2.6.2
1
Yes
Yes
7.9.2.4.4 and
7.9.4.2.3.4
and
7.9.2.6.2.3.2
7.9.4.2.5.2.3.3
criteria Met?
met?
Criteria
No
No
No
2
Preliminary
IsPulsation
pulsation
Is
supression device
Suppression
Device
design to
to be
be complete
design
complete
and
final
before
and final before
completion of
of piping
completion
piping
layout?
No
No
Preliminary
piping
Pi i
layout complete?
Complete?
Yes
Perform
Perform
Pre-Study
pre-study
per 7.9.4.2.3.4
7.9.2.4.4
per
Revise
Revise
dampener
Dampener
design
Design
layout?
Yes
Yes
Pulsation
PulsationSuppression
suppression
Device
devicedesign
designisisfinal
finaland
and
released
forfororder.
released
order. Future
Future
design
changescan
canonly
onlybe
be
design
changes
made
thepiping
pipingsystem.
system.
made
totothe
Completepiping
piping
Complete
systemdesign
design
system
andlayout.
layout.
and
Perform
PerformAcoustic
acoustic
Simulation per
per 7.9.2.4.5
simulation
7.9.4.2.3.5
3
Revise
Revise
design
Design
Pulsation Criteria
Pulsation
criteria
7.9.2.6.2.1 and
7.9.4.2.5.2.1
and pressure
7 pressure
9 2 6 2 2 drop criteria
drop criteria 7.9.4.2.5.3.1
7.9.2.6.3.1 and Compressor
and
compressor system
System shaking force
shaking
force criteria
criteria
7.9.2.6.2.3.2
M t?7.9.4.2.5.2.3.3.
Yes
Yes
Complete
Piping
CompleteMaximum
maximum
piping
Span
spanTable
tableand
andVessel
vessel
Mechanical
mechanicalNatural
natural
Frequency
frequencyCalculations
calculationsper
per
7.9.2.4.6
7.9.4.2.3.6.
4
No
(see
No
Note)
(see
Note)
No
No
Is Is
Separation
separationMargin
margin
criteria in 7.9.4.2.5.3.2
Criteria
7.9.2.6.3.2
met?
met?
Yes
Yes
Design
Approach
Design
approach2 2isis
complete.
complete.No
Nofurther
further
analysis
is is
required.
analysis
required.
Note: In the event that pulsation suppression device design is fixed, it may be necessary to accept higher pressure drop or perform a Design
Approach 3 analysis.
Figure M-2—Design Approach 2
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
Preliminary pulsation suppression device sizing per
7.9.4.2.2. If specified, minimum volume shall be per
7.9.3.2.
X
Yes
7.9.4.2.3.4 and
7.9.4.2.5.3.1c
criteria met?
Shows the step in 7.9.4.2.5.2
No
No
Yes
Perform acoustic
simulation per 7.9.4.2.3.5
Revise
pulsation
suppression
device or
piping
system
design
(see Note 3)
No
Preliminary piping
layout complete?
Pulsation criteria
7.9.4.2.5.2.1 and 7.9.4.2.5.2.2.2
and pressure drop criteria
7.9.4.2.5.3.1 met?
Revise
dampener
design
Yes
Perform
pre-study per
7.9.4.2.3.4
Complete
piping
system
design
and
layout.
Yes
No
Can the pulsation
criteria be met by
exceeding the
pressure drop criteria
in 7.9.4.2.5.3.1c?
(see Note 2)
No
Has allowance to
exceed the pulsation
criteria in 7.9.4.2.5.2.1 or
7.9.4.2.5.2.2.3 been
agreed upon?
(see Note 1)
Yes
No
Is the pulsation
suppression device
design to be
completed before
completion of
preliminary piping
layout?
Has allowance to
exceed the pressure
drop criteria in
7.9.4.2.5.3.1c been
given to enable
compliance with the
pulsation criteria?
No
Pulsation
suppression
device design is
final and released
for order. Future
design changes can
only be made to
the piping system.
Yes
Step 3a
mechanical analysis
of compressor system
and piping system per
7.9.4.2.4.2
Revise pulsation
suppression
device and/or
piping system
and/or structural
support design
(see Note 3)
Yes
Note 1—The default design philosophy is
pressure pulsation control unless otherwise
specified. However, when evaluating the
need for possible modification to the piping
and/or pulsation suppression devices,
consideration should be given to acousticalshaking forces and the effect of pulsations on
compressor performance. Also, pulsation
levels (expressed as a percentage of line
pressure) should not be used as the sole
criterion for making modifications.
And
No
Revise
pulsation
suppression
device and/or
piping system
and/or
structural
support
Compressor
system
separation
margin driteria
7.9.4.2.5.3.2 met?
Yes
And
No
Compressor
system shaking
force criteria
7.9.4.2.5.2.3.3 met?
(see Note 4)
Yes
Yes
Piping system
separation
margin criteria
7.9.4.2.5.3.2 met?
No
And
Yes
Piping system
shaking force
No
criteria
7.9.4.2.5.2.3.3 met?
(see Note 4)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Note 3—When design revisions are complete,
the flowchart indicates that the acoustic
simulation is run again. In practice, if the
revisions (for example, structural support
changes) do not impact the acoustic
simulation, then the previous simulation is still
valid. In this case, the evaluation of the
design change would begin with Step 3a;
; but,
,
the designer is responsible for ensuring that
the acoustic simulation is still valid. Also, note
,
that not all options for design revisions listed
(for example, modifying the pulsation
suppression device) will be available
depending upon decisions that have already
been made.
Or
Or
Step 3b1
Perform forced mechanical response
analysis on compressor mechanical model
per 7.9.4.2.4.3
Step 3b
Perform forced mechanical response
analysis on piping system per 7.9.4.2.4.4
Yes
Vibration and cyclic stress
criteria 7.9.4.2.5.2.5.1 met?
(see Note 5)
No
Note 2—For some applications that have
variable operating parameters such as speed
or gas composition, it may not be technically
possible oreconomically
economicallyfeasible
feasibletoto
simultaneously comply with the pulsation and
the pressure drop limitations for all operating
conditions. The purchaser and designer
should mutually agree upon the most
appropriate compromise.
Yes
Piping system
vibration criteria
7.9.4.2.5.2.4 met?
Revise
design
No
Yes
Cyclic stress criteria
7.9.4.2.5.2.5.1 met?
No
Design approach 3 is complete. No
further analysis is required.
Figure M-3—Design Approach 3
Note 4—The requirement to analyze the
shaking forces in Step 6 is waived if the
compressor vendor analyzes the piping
system vibration in Step 7 per 7.9.4.2.4.4. If the
7.9.4.2.4.4
shaking forces are not analyzed, then “No” is
selected and analysis proceeds to Step 7.
Note 5—The compressor vendor shall supply
the allowable vibration criteria for compressor
components such as cylinders, distance
pieces and crankcases. Due to the variability
and complexity of compressor systems, it is
not possible to provide vibration criteria that,
when met, eliminate the need to calculate
stress. ,
175
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Annex N
(informative)
Guideline for Compressor Gas Piping Design and Preparation for an
Acoustic Simulation Analysis
N.1 General
N.1.1 Any reciprocating compressor in conjunction with a piping system forms an interactive dynamic system that cannot be
accurately analyzed as two separate systems. Therefore, it is virtually impossible for the pulsation system designer and the piping
system designer to arrive at proposed designs on an independent basis that can be guaranteed to work in the final analysis and be
cost effective.
N.1.2 This annex gives guidelines for the piping system designer which will help to minimize problems that can occur at the
time of the acoustic simulation and it also outlines the information that must be available at the time of this interactive analysis.
Communication between the piping system designer, the compressor vendor and the pulsation control system designer during the
course of a project is important to minimize problems and develop the best overall compressor system installation. The key times
of interaction are at the post order coordination meeting (see 9.1.3), early in the project, and during the interactive acoustic
simulation/mechanical analysis.
N.1.3 The purchaser may elect to perform an in-house acoustic simulation, to use equipment vendor services or to use the
services of a third party.
N.2 Acoustic Consideration in Piping Designs
N.2.1 The interaction of the compressor, pulsation devices and piping system produces potentially harmful pulsations when
there is resonant interaction between the various elements in the system. The system designer can help to minimize this
interaction by avoiding resonant lengths of pipe. When resonant lengths of pipe are used and the resonant frequency matches
compressing frequency, one can expect major changes to the system as a result of the acoustic simulation analysis. The resonant
length of various piping configurations is given in Equation N-1. It is recommended that lengths of these configurations be
avoided in a ±10% band for the first four harmonics of compressor speed. The piping areas where this is most important are the
sections of piping between the first major volume on the suction side and the first major volume on the discharge side. In piping
areas outside major volumes, or those far enough away from the compressor(s) the potential for harmful pulsation buildup is
considerably reduced.
N.2.2 For piping sections open at both ends or closed at both ends the length to be avoided can be calculated from the
following:
30c
L H = -------nN
(N-1)
where
LH
is the pipe length to be avoided in meters (feet);
C
is the velocity of sound in gas in meters/second (feet/second);
n
is the harmonic number (1, 2, 3 and 4);
N
is the compressor speed in revolutions per minute.
Examples of this are lengths between major volumes, length of headers, etc.
N.2.3 For pipe sections open at one end and closed at the other end, the lengths to be avoided can be calculated from the
following:
177
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178
API STANDARD 618
15C
L Q = ---------nN
(N-2)
where
LQ
is the pipe length to be avoided in meters (feet);
C
is the velocity of sound in gas in meters/second (feet/second);
n
is the harmonic number (1, 2, 3 and 4);
N
is the compressor speed in revolutions per minute.
Examples of this are relief valve lines and bypass lines.
Note: A pipe can be considered to have an open end if the diameter increases by a factor of 2 to 1 or more. Similarly, a pipe can be considered to
have a closed end if the diameter is reduced by a factor of 2 to 1 or more.
N.2.4 The acoustic simulation should be carried out after a piping static stress analysis has demonstrated that the location and
design of the piping restraints result in acceptable piping static stresses.
N.2.5 For variable speed compressors and/or those with varying gas composition and/or varying pressures and temperatures,
the separation of resonances is more difficult to calculate and can only be handled properly with an acoustic simulation study.
N.3 Acoustic simulation study
N.3.1 The extent of the piping system to be analyzed by acoustic simulation techniques is usually defined as all associated
piping systems to a point where piping changes will have only insignificant effects on the parts of the system under study and in
determining the acoustic characteristics of the design. Typically, these requirements are satisfied by beginning the simulation with
the inlet of a major process vessel or volume on the suction side of the compressor unit(s), continuing through all interstage
systems (if any) and terminating the study at the outlet of a major process vessel or volume on the discharge side of the unit(s).
Included are branch connections to or from this system, such as relief valve lines and bypass lines.
N.3.2 When major volumes do not exist or are very remote from the compressor, suitable piping lengths are included in the
simulation, such that the pulsation levels are sufficiently low so as to minimize the potential of pulsation driven vibration
problems.
N.4 Information required
N.4.1 The acoustic simulation requires a considerable amount of information in order to be properly performed. The purchaser
and the vendor should agree upon who is responsible for the development and compilation of the following information:
N.4.1.1 Data sheets showing all compressor operating conditions, analysis of all gases to be compressed, and all unloading
steps.
N.4.1.2 Isometric drawings showing all lengths (between bends, valves, diameter changes, etc.) and line sizes and schedules
for the complete piping system, including all branch lines and relief valve lines. If a mechanical study is included, the distance
between the supports and the type of support and clamp used at each location must be shown on the isometrics. A detailed
drawing of each type of support and clamp is required.
N.4.1.3 Piping and instrument diagrams (P&ID’s) are required to ensure that all piping and equipment that may effect the study
are included.
N.4.1.4 Layout drawings are required to help determine the practicality of any proposed modifications. Reproducible drawings
are useful since they can be marked up and copies can be included in the report.
N.4.1.5 Complete information must be supplied on all of the piping up to and including the first large volume in the suction, the
interstage and the discharge piping. Every branch must be included up to a shutoff valve or a large volume.
N.4.1.6 Any orifice or other flow-resistive device must be shown and complete details provided.
N.4.1.7 Detailed drawings of each vessel, showing the location of all nozzles, the internal diameter and the length, as well as
details of any vessel internals are required. Normal liquid levels and design pressure drops in these vessels must be shown.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
179
N.4.1.8 TEMA data sheets, or their equivalent, must be provided for all heat exchangers. The data sheets must show whether
gas is through the tubes or in the shell; the number, length and gauge of tubes; whether the tubes are plain or finned; the number
of passes; the I.D. of the shell; the gas temperature in and out; the gas pressure drop; and the dimensions of the header. A
dimensional drawing is preferred.
N.4.1.9 If there are different gas routings, a complete description must be included to show the relative positions of all the
valves for each routing. If different process gases are involved, the description must show which routings apply to which gases.
Flow from/to any sidestream must be shown, including gas analysis, flow rate and direction.
N.4.1.10 If gas filters are used, the type of filter, internal diameter, length and element pressure drop must be supplied. A
dimensional drawing is desirable.
N.4.1.11 When two or more compressors are connected to the same piping system, a clear description of how they will operate
(such as unloading steps, speed differences, etc.) is required.
N.4.1.12 Detailed dimensional drawings on each suppressor showing the location of all nozzles, lengths, internal diameters and
details on suppressor internals, if any.
N.4.1.13 The information in Table N.1 is required from the compressor vendor.
Table N-1—Compressor Data Required for Acoustic Simulation
Design Approach
23a, 3b1, 3b2
Compressor Data
Compressor data
Head end fixed clearance volume
Head end unloader volume(s)
Crank end fixed clearance volume
Crank end unloader volume(s)
Casting drawings
Compressor cylinder (internal passage)
Distance piece (inertia and stiffness)
Crosshead guide (inertia and stiffness)
Assembled cylinder weight
Support drawings
Cylinder support drawings
Crosshead guide support drawings
Distance piece support drawings
Pulsation suppressor support drawings
Compressor Dynamic Valve Analysis Results
Crank angles between manifolded cylinders
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
X
N.4.2 It is highly recommended that a piping system design representative who is familiar with the piping system be present at
the acoustical simulation analysis, in order to make piping changes as the need arises.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Annex O
(informative)
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Guidelines for Sizing Low Pass Acoustic Filters
O.1 General
The general configuration for an acoustic filter is shown in Figure O-1.
$C
6
6
,
,C
,
Figure O-1—Nonsymmetrical Filter
The lowest acoustic resonant frequency of the filter system, is referred to as Helmholtz frequency (fH). An accepted generalized
equation for Helmholtz frequency is
1
--c ⎛ μ μ ⎞2
f H = ------ ----- + ----(O-1)
2π ⎝ V 1 V 2⎠
where
fH
c
is the Helmholtz frequency in Hertz;
is the velocity of sound in gas in meters per second (feet per second);
V1
is the volume in cylinder bottle (chamber) in cubic meters (cubic feet);
V2
is the volume in filter bottle (chamber) in cubic meters (cubic feet);
μ
is the acoustic conductivity in meters or feet.
where
A
A
μ = ------------------------- = --L
L c + 0.6D c
A
is the internal cross-sectional area of choke in square meters (square feet);
Lc
is the actual length of choke in meters (feet);
L
Dc
is the acoustic length of choke in meters (feet);
is the diameter of choke in meters (feet).
The filter cut-off frequency (fco), which is the frequency above which pulsation attenuation is achieved, is usually defined as
follows
f co = ( 2 )f H
The acoustic filter can be either symmetrical or non-symmetrical. As shown in Figure O-1 and Equation 1, the non-symmetrical
filter can have different volumes (lengths and diameters) and a different length of choke. For a symmetrical filter, the volumes are
181
182
API STANDARD 618
equal and the acoustic length of the choke L is equal to the length of each volume that is Lc = L. This is valid when Lc is much
larger than Dc. This also means that the diameter of each volume is equal.
Substituting into Equation O-1, the Helmholtz frequency for a symmetrical filter becomes:
1 c Dc
f H = ------- --- --------2 π LD B
where
(O-2)
DB = inside diameter of pulsation suppression devices in meters (feet).
O.2 Guidelines
The following guidelines may be used for the preliminary sizing of acoustic filters.
O.2.1 SELECTION OF HELMHOLTZ FREQUENCY (FH)
The preferred Helmholtz frequency is:
s
f H = -----85
where
s
is the compressor speed in r/min.
Only when conditions are such that it is uneconomical, or physically impractical, should a higher Helmholtz frequency be
considered, that is, only when pressure drop is very critical—as in the case of low suction pressure, or when space is limited by
the compressor system layout. In that instance, a higher Helmholtz frequency may be chosen. Generally, the Helmholtz frequency
should not be higher than
s
f H = -----45
unless the acoustic simulation proves otherwise. For compressor speeds above 500 rpm, the Helmholtz frequency should not
exceed:
s
f H = -----85
O.2.2 RELATIONSHIPS OF FILTER ELEMENT DIAMETERS
For acoustic considerations, the diameter of the cylinder bottle (chamber) V1 should be equal to, or greater than, two times the
diameter of the cylinder connection (flange). Larger ratios generally improve acoustic characteristics but may result in
unacceptable mechanical characteristics. The final design ratio must be determined by both acoustic and mechanical analysis.
The diameter of the filter bottle (chamber) V2 should be equal to, or greater than, three times the diameter of the line piping.
O.2.3 RELATIONSHIP OF FILTER ELEMENT LENGTHS
The preferred filter system is with equal lengths of cylinder bottle (chamber), choke tube and filter bottle (chamber) that is
L1 = LC = LZ. In cases where the physical restrains (piping layout) and the required sizes do not permit equal lengths, the next best
alternative is with equal length of choke and filter (chamber) L1 ≠ LC = L2.
O.2.4 SIZING OF THE DIAMETER OF THE CHOKE TUBE (DC)
Unless otherwise specified, calculate the maximum allowable pressure drop per the applicable Equation 13 in 7.9.4.2.5.2.3.2.
Using maximum allowable pressure drop and appropriate pressure drop relationship, calculate the minimum diameter choke tube
which can be used considering all operating conditions expected.
O.2.5 ACOUSTIC SIMULATION OF THE PRELIMINARY DESIGN
These sizing guidelines cannot be used to determine the final dimensions of the filter elements without an acoustic simulation.
Once the preliminary design of the filter is completed, an acoustic simulation must be performed to evaluate the unbalanced
shaking forces within the components of the filter and the pulsation levels at the nozzles. Adjustments to the filter component
dimensions are almost always made during the acoustic simulation.
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Annex P
(informative)
Piping and Pulsation Suppression Device Shaking Force Guidelines
P.1 General
Shaking force guidelines provide an alternative evaluation tool to determine the need for forced mechanical response analysis.
The foundation for deriving appropriate shaking force guidelines is knowledge of stiffness and acceptable vibration for the
structure. Knowledge of the structure’s stiffness may be based on experience with similar structures, or based on calculation
varying in precision from assuming minimum stiffness values to stiffness determined by detailed structural simulation. Similarly,
knowledge of acceptable vibration may be experience based or determined by detailed structural modeling.
The adopted shaking force guidelines work in concert with the separation margin and the design vibration guidelines. The
simplification to a non-resonant shaking force guideline requires simultaneous compliance with both the shaking force and
separation margin guidelines.
Figure P-1 shows the piping non-resonant shaking force guideline versus a corresponding shaking force guideline accounting for
resonance. The non-resonant shaking force guideline results in acceptable vibration when the separation margin guidelines are
met. Meeting both the minimum natural frequency guideline and the non-resonant shaking force guideline ensures acceptable
vibration for the first and second orders of compressor speed. Meeting both the 20% separation margin from natural frequencies
and the non-resonant shaking force guideline will also ensure acceptable vibration at higher orders of compressor speed.
Therefore, the piping non-resonant shaking force guideline applies when the separation margin guidelines are met. When the
separation margin guidelines are not met, much lower piping shaking forces are required to ensure acceptable vibration.
Figure P-2 shows the pulsation suppression device non-resonant shaking force guideline versus a corresponding shaking force
guideline accounting for typical resonance. As with the piping, the pulsation suppression device non-resonant shaking force
guideline applies when the separation margin guidelines are met. When the separation margin guidelines are not met, much lower
pulsation suppression device shaking forces are required to ensure acceptable vibration.
Figures P-1 and P-2 demonstrate the importance of meeting the separation margins when applying the non-resonant shaking force
guidelines.
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5HVRQDQW
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Figure P-1—Non–dimensional Piping Shaking Force Guidelines
183
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184
API STANDARD 618
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6)
.
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Figure P-2—Non-dimensional Pulsation Suppression Device Shaking Force Guidelines
P.2 Orientation of Shaking Forces
P.2.1 PIPING ORIENTATION
The piping non-resonant shaking force guideline applies to shaking forces acting along the piping axis, as shown in Figure P-3,
which cause non-resonant vibration. The piping non-resonant shaking force guideline cannot be applied when resonant vibration
occurs in either the run containing the shaking force or in adjoining perpendicular piping.
Axial Vibration
Transverse
Vibration
Axial Shaking Force,
Axial Stiffness
Figure P-3—Shaking Forces along the Piping Axis
P.2.2 CYLINDER MOUNTED PULSATION SUPPRESSION DEVICE ORIENTATION
The pulsation suppression device non-resonant shaking force guideline applies to shaking forces acting along the pulsation
suppression device axis, as shown in Figure P-4, which cause non-resonant vibration.
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RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
Shaking Force, Vibration
185
Shaking Force,
Vibration
Suction Pulsation
Suppression Device
Cylinder
Cylinder
Discharge Pulsation
Suppression Device
Shaking Force,
Vibration
Shaking Force, Vibration
Figure P-4—Shaking Forces along the Pulsation Suppression Device Axis
P.3 Determination of Effective Static Stiffness
P.3.1 GENERAL
Suggested equations for effective stiffness of piping and pulsation suppression devices are provided in P.3.2 and P.3.3. In addition,
meeting the minimum mechanical natural frequency guideline can be used to establish a required minimum effective static
stiffness. Equations for minimum effective static stiffness of piping and pulsation suppression devices are also given below.
P.3.2 PIPING EFFECTIVE AND MINIMUM STATIC STIFFNESS
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P.3.2.1 The effective axial stiffness of piping is usually determined by the axial stiffness of the supports as shown in Equation
P-1.
k eff = 0.66 × n × k s
.
(P-1)
where
keff
0.66
is the effective static stiffness along the piping where the shaking force acts in N/mm (lbf/in.);
is the dynamic design factor to account for reduced stiffness as resonance is approached (see Figure P-1);
n
is the number of active axial supports (see P.2.1.1 when supports are not collinear with the pipe run where the
shaking force is acting);
ks
is the axial static support stiffness in N/mm (lbf/in.).
To satisfy the minimum natural frequency guideline (see clause 7.9.4.2.5.3.2), the active axial support stiffness must at least meet
the minimum ks defined in Equation P-2. Equation P-2 satisfies the minimum required support stiffness for all practical piping
configurations with maximum acceptable spans (see P.2.1.2 and P.2.1.3 regarding lumped masses and equipment).
minimum k s = C KS × A
0.75
×I
0.25
1.5
× f n,T ( n – 1 ⁄ n )
(P-2)
186
API STANDARD 618
where
CKS
A
is the constant dependent on support stiffness units (SI units: 1/130; USC units: 25);
is the pipe cross-sectional metal area in mm2 (in.2);
= π/4 × (OD2 – ID2);
I
is the pipe cross-sectional area moment of inertia in mm4 (in.4);
= π/64 × (OD4 – ID4);
OD
is the pipe outer diameter in mm (in.);
ID
is the pipe inner diameter in mm (in.);
fn,T
is the minimum transverse natural frequency in Hz (see P 3.2.5);
n
is the number of active supports (or n = 2 as a minimum, see P 3.2.7).
The actual value of ks should be determined and compared to the minimum ks requirement. When the actual ks is greater than
minimum ks there is sufficient support stiffness to constrain higher shaking forces (up to the limit defined by Equation 10 in
7.9.4.2.5.2.3.2 and P.1). When the actual ks is lower than minimum ks, the minimum mechanical natural frequency separation
margin guideline will not be met, and the possibility of operating on resonance within the first two orders of compressor speed
must be considered.
The actual and minimum ks values should also be compared with the range of typical support stiffness values found in Note 2 of
7.9.4.2.5.2.3. The actual ks should fall within the range of the corresponding support type. When the minimum ks required
exceeds the range of the corresponding support type, the actual ks must be carefully determined and either a sufficiently stiff type
of structure must be used or the shaking force guideline must be reduced.
P.3.2.2 When supports are not collinear with the pipe run where the shaking force is acting (such as the middle section of U, Z
or 3D bends), the perpendicular pipe sections clamped by the supports may be more flexible than the supports, and keff must
correspondingly be reduced. Flexibility of the perpendicular pipe section should be considered when the support is offset greater
than 25% of the maximum acceptable span length.
P.3.2.3 The calculation of minimum ks does not include lumped masses, but results in a conservative shaking force criteria
when the separation margin minimum natural frequency guideline is satisfied. To ensure the separation margin criteria are
satisfied, the support requirements of each lumped mass, such as valves, must additionally be provided.
P.3.2.4 The calculation of minimum ks is based on the minimum number of supports required to satisfy the minimum
mechanical natural frequency guideline. When more than the minimum number of supports are present, the minimum ks can be
reduced by the ratio of the minimum number required divided by the number of active supports.
P.3.2.5 The minimum transverse natural frequency (fn,T) required is dependent on the frequency of the shaking force. For
example, to comply with the first part of the separation margin criteria, it is typically chosen as 2.4 times maximum rated speed.
In higher speed compressors, this is not always practical to achieve, however Equation P-2 can still be used to determine the
minimum support stiffness required for the given fn,T.
P.3.2.6 The minimum axial support stiffness requirements of vessels and equipment (such as secondary pulsation dampeners,
separators, cooler sections and heat exchangers) should be determined directly from the equipment mass to meet the separation
margin criteria.
P.3.2.7 The number of active supports include all axial restraints along the run containing the shaking force and restraints offset
from the run less than 25% of the maximum acceptable span length.
P.3.2.8 Vessels and equipment may also be restraints. See examples in Figure P-5.
P.3.2.9 Pipe wall thickness is specified based on design pressure using applicable design codes and is not increased as a method
to control vibration.
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n=3
Shaking Force
L = Lspan / 4
Shaking Force
Shaking Force
RECIPROCATING COMPRESSORS FOR PETROLEUM, CHEMICAL, AND GAS INDUSTRY SERVICES
L = Lspan / 4
n=3
187
L = Lspan / 4
n=3
Figure P-5—Examples of Shaking Force Restraints
P.3.3 CYLINDER MOUNTED PULSATION SUPPRESSION DEVICE EFFECTIVE AND MINIMUM STATIC
STIFFNESS
The effective axial stiffness of cylinder mounted pulsation suppression devices is the result of a complex interaction between
many structures requiring detailed analysis or field measurement to determine. Expressed in the same form as the effective
stiffness for piping yields Equation P-3.
k eff = 0.66 × k t
(P-3)
where
keff
0.66
kt
is the effective static stiffness along the pulsation suppression axis where the shaking force acts in N/mm (lbf/in.);
dynamic design factor to account for reduced stiffness as resonance is approached (see Figure P-2);
is the pulsation suppression device axial static support stiffness in N/mm (lbf/in.).
Noting that the cylinder assembly stiffness is a critical component of the pulsation suppression device stiffness, and considering
reasonable supporting of typical cylinder assemblies, a minimum kt can be established based on the number of cylinders as shown
in Equation P-4.
minimumkt = k min × n cyl
where
kmin
is the minimum pulsation suppression device axial static stiffness per cylinder nozzle (SI units: 50 × 103 N/mm;
USC units: 3 × 105 lbf/in.);
ncyl
is the number of cylinders attached to pulsation suppression device.
CAUTION: Long cylinder nozzles, double compartment and small cross-section distance pieces may not provide the minimum
axial stiffness.
Also, on higher speed units, larger and higher pressure cylinders may require greater than the minimum axial stiffness to meet the
minimum natural frequency guideline. Cylinders heavier than shown in Table P-1 may require additional supporting.
Table P-1—Cylinder Assembly Weights Possibly Requiring Strengthening
Maximum Compressor Speed (rpm)
Cylinder Assembly Weight (N)
Cylinder Assembly Weight (lbf)
300
89000
20000
600
22000
5000
900
9800
2200
1000
8000
1800
1200
5500
1250
1500
3500
800
The maximum cylinder assembly weight for compressor speeds not shown in the Table P-1 can be obtained using Equation P-5.
W cyl = C c ⁄ S
.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
2
188
API STANDARD 618
where
Wcyl
Cc
S
is the maximum cylinder assembly weight in N (lbf);
is the constant dependent on weight and stiffness units (SI units: 8.0 × 109; USC units: 1.8 × 109);
is the compressor rotational speed in r/min.
P.4 Evaluation of Shaking Forces
Making modifications to reduce predicted shaking forces is referred to as shaking force control (see API RP 688 for a complete
discussion of the various control methods). As a minimum, shaking force control is required for all cylinder mounted pulsation
suppression devices. When the purchaser agrees, shaking force control may be used in place of piping pressure pulsation
guidelines.
The first step in the shaking force control method is to determine the shaking force guidelines using the equations and methods
shown in 7.9.4.2.5.3 and Annex P. Then, the predicted shaking forces are compared to the shaking force and separation margin
guidelines. When predicted shaking forces do not meet these guidelines, then one or more of the following actions must be taken
to obtain acceptable results:
—modify system acoustics to reduce predicted shaking forces;
—modify support structure to meet separation margin guidelines;
—perform forced mechanical response analysis and satisfy vibration guideline.
--``,,,``,,`````,``,,,,,,,`,,`,,-`-`,,`,,`,`,,`---
Combinations of the above options are often employed in an iterative fashion to arrive at acceptable predicted shaking forces for
the entire system.
Annex Q
(informative)
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Compressor Components—Compliance with NACE MR0175
189
Spacer
Intermediate partition
packing
Oil slinger
Spacer
Notes:
1. All parts shown not sectioned are required by 6.15.1.11 to be NACE MRO175 material. All
parts shown sectioned
are not required to be NACE materials.
2. Applying NACE exposure guidelines allow the use of non-NACE bolting materials for
external fasteners on the cylinder and internal fasteners within the distance pieces.
3. See Figure J-1 for reciprocating compressor nomenclature.
Oil wiper
packing
Pressure
packing
O-ring type valve cover
Port or plug type unloader
Finger type valve unloader
Clearance
pocket
unloader
190
API STANDARD 618
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Figure Q-1—Material Guidelines for Compressor Components—Compliance with NACE MR0175
Date of Errata Issue: November 2009
Affected Publication: API Standard 618, Reciprocating Compressors for Petroleum, Chemical,
and Gas Industry Services, Fifth Edition, December 2007
This errata corrects editorial errors in the fifth edition of API 618.
Page 139, Annex F, F.1, insert the following VDDR forms:
1
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ERRATA 1
TYPICAL
VENDOR DRAWING AND
DATA REQUIREMENTS
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DATE
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DATE
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DATE
1
FOR
REVISION
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NO. REQUIRED
Proposal a
Review
Final
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a
b
c
c
b
OF
2
BY
Bidder shall furnish
copies of data for all items indicated by an X.
Vendor shall furnish
copies and
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Vendor shall furnish
copies and
transparencies of drawings and data indicated.
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DISTRIBUTION
RECORD
transparencies of drawings and data indicated.
Final-Received from vendor
c
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DESCRIPTION
Proposal drawings and data do not have to be certified or as-built. Typical data shall be clearly identified as such.
Purchaser shall indicate in this column the timeframe for submission of materials using the nomenclature given at the end of this form.
Bidder shall complete these two columns to reflect their actual distribution schedule and include this form with their proposal.
JOB NO.
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DATA REQUIREMENTS
Proposal
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Final
c
a
PAGE
ITEM NO.
2
OF
DATE
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BY
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Bidder shall furnish
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Vendor shall furnish
copies and
Vendor shall furnish
Vendor shall furnish
copies and
transparencies of drawings and data indicated.
operating and maintenance manuals.
transparencies of drawings and data indicated.
Final-Receive from vendor
c
Final-Due from vendor
Review-Returned to vendor
Review-Received from vendor
c
Review-Due from vendor
DISTRIBUTION
RECORD
DESCRIPTION
a
b
c
Proposal drawings and data do not have to be certified or as-built. Typical data shall be clearly identified as such.
Purchaser shall indicate in this column the timeframe for submission of materials using the nomenclature given at the end of this form.
Bidder shall complete these two columns to reflect their actual distribution schedule and include this form with their proposal.
Notes:
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Vendor
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(Signature acknowledges receipt of all instructions)
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